CN106186443A - Oily waste water integrated treatment unit - Google Patents
Oily waste water integrated treatment unit Download PDFInfo
- Publication number
- CN106186443A CN106186443A CN201610754239.7A CN201610754239A CN106186443A CN 106186443 A CN106186443 A CN 106186443A CN 201610754239 A CN201610754239 A CN 201610754239A CN 106186443 A CN106186443 A CN 106186443A
- Authority
- CN
- China
- Prior art keywords
- zone
- clear water
- settling
- oily waste
- waste water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 239000010802 sludge Substances 0.000 claims abstract description 30
- 238000005188 flotation Methods 0.000 claims abstract description 28
- 239000002893 slag Substances 0.000 claims abstract description 17
- 238000007790 scraping Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 4
- 238000005352 clarification Methods 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims 2
- 239000000945 filler Substances 0.000 abstract description 13
- 238000001556 precipitation Methods 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 6
- 238000004891 communication Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 241000238634 Libellulidae Species 0.000 description 5
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 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
- C02F1/40—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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
-
- 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
- C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
-
- 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
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
- C02F2103/365—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds from petrochemical industry (e.g. refineries)
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- 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
- C02F2301/04—Flow arrangements
-
- 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)
- Removal Of Floating Material (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention belongs to sewage treatment area, a kind of oily waste water integrated treatment unit, including the oil interceptor set gradually, reactor, contact area, clear water zone and settling section, baffle interval is passed through between contact area, clear water zone and settling section, contact area includes air flotation zone and settling zone, air flotation zone one upper lateral part connects with settling zone, is provided with the release head connected with dissolving bottom air flotation zone, reactor by pipeline communication to bottom air flotation zone；Top, settling zone is provided with Slag Scraping Device, is provided with the first inclined tube filler in the middle part of it, is provided with the first tapered sludge bucket bottom it；Settling zone one side bottom connects with clear water zone, and top, clear water zone connects with settling section；It is provided with the second inclined tube filler in the middle part of settling section, bottom it, is provided with the second tapered sludge bucket.The application plant area area is little, and space availability ratio is high, and the oil can efficiently removed in oily waste water through processes such as oil skimming, dosing reaction, air supporting, two-step precipitations divides.
Description
Technical field
The invention belongs to sewage treatment area, particularly relate to a kind of oily waste water integrated treatment unit.
Background technology
The industry such as petroleum and petrochemical industry, food produces a large amount of oily waste waters, and the oil content dispersion and emulsion in these oily waste waters is at water
In, it is difficult to remove.A large amount of oiliness sewage treatment are not thorough, and direct discharge can cause the wave of serious water environment pollution and water resource
Take.For making the abundant process of oil point in waste water, it usually needs multiple equipment process, and floor space is bigger.
Summary of the invention
It is an object of the invention to overcome prior art to there is the defect that oiliness sewage treatment occupation area of equipment is big, it is provided that one
Plant oily waste water integrated treatment unit.
The technical solution adopted for the present invention to solve the technical problems is: a kind of oily waste water integrated treatment unit, bag
Include oil interceptor, reactor, contact area, clear water zone and the settling section set gradually, between described contact area, clear water zone and settling section
By baffle interval, described contact area includes air flotation zone and settling zone, and described air flotation zone one upper lateral part is with described settling zone even
Logical, it is provided with the release head connected with dissolving bottom described air flotation zone, described reactor is by pipeline communication to described air supporting
Bottom district；Top, described settling zone is provided with Slag Scraping Device, is provided with the first inclined tube filler, is provided with tapered bottom it in the middle part of it
The first sludge bucket；Described settling zone one side bottom connects with described clear water zone, and top, described clear water zone is with described settling section even
Logical；It is provided with the second inclined tube filler in the middle part of described settling section, bottom it, is provided with the second tapered sludge bucket.
Further, it is provided with oil skimmer in described oil interceptor, in described reactor, agitating device is set.Utilize oil skimmer
The oil that can tentatively skim in oily waste water divides, and oily waste water is added thereto to the medicaments such as flocculant after entering reactor, utilizes
Agitator can effectively make medicament be fully contacted with oily waste water, fully reacts.
As preferably, described top, contact area is provided with dirt colleceting area, and described dirt colleceting area sets near side, described air flotation zone
Put.Will be arranged on water inlet one end, contact area in dirt colleceting area, Slag Scraping Device flow path direction against the current will swim in the dirt scraping on sewage top extremely
Dirt colleceting area, owing to the slag body being in the sewage on top, air flotation zone floating is more, and produces very fast, and inversely scraping slag can be rapidly and efficiently
Slag body is scraped to dirt colleceting area by ground so that the slag body floating away from the side of water inlet end is less, is simultaneously also beneficial to oily waste water and exists
Settling zone precipitates.
Further, it is provided with sludge outlet bottom described contact area and settling section.Utilize the sludge outlet can be effective
Mud between first sludge bucket and between the second sludge bucket is discharged.
As preferably, bottom described settling zone, the side near described clear water zone is provided with deflection plate, described deflection plate
Bottom is obliquely installed towards described clear water zone.Deflection plate can effectively mud block avoid its enter clear water zone, after precipitation
Clear water is walked around deflection plate and is entered clear water zone, it is possible to effectively reduce clear water zone pollutant load.
As preferably, in described clear water zone, be provided with out water regulator, described in go out water regulator and include adjusting rod and setting
Putting the block bottom described adjusting rod, described block seals with described clear water zone side walls and arranges, and described block is described
The liquid level moved up and down in clear water zone thus control in clear water zone.When block upward sliding, in clear water zone, liquid level rises, precipitation
District and settling section water level decline accordingly, block slide downward, and in clear water zone, liquid level declines, on settling zone and settling section water level are corresponding
Rise, utilize out the water level that water regulator can effectively regulate in clear water zone, thus control settling zone and settling section water level, thus have
It is beneficial to settling zone and scrapes slag, it is to avoid in settling zone, liquid level is too high or too low causes Slag Scraping Device to scrape the inefficient problem of slag.
As preferably, described settling section top is provided with overflow launder, and described second sludge bucket is internal is hollow structure, wherein
Hollow structure forms intermediate pool, described overflow launder by connect with described intermediate pool communicating pipe, described intermediate pool pass through air tube and
Extraneous connection, described intermediate pool is provided with drain pipe.The inner space utilizing the second sludge bucket forms intermediate pool, after clarification
Clear water is collected within it, can be carried out continuously lifting work by pump, and only utilize overflow launder little due to its discharge capacity, promote with pump
Time, pump can not work continuously, and vaccuum phenomenon easily occurs, shortens the service life of pump；Intermediate pool is positioned at settling section simultaneously
Internal, it is not necessary to the extra installing space increasing equipment, take full advantage of space, improve space availability ratio；Due to intermediate pool
For airtight space, being passed through water the most wherein can utilize the air tube can owing to, under pressure effect, water will not enter intermediate pool
Pressure in active balance intermediate pool so that the water in overflow launder can enter intermediate pool smoothly.
As preferably, also include the air compressor machine connected with outside air connected with described dissolving and connect with clear water zone
Reflux pump.By the water circulation use after preliminary treatment of clear water zone, it is to avoid introduce new water body, beneficially using water wisely,
Alleviate the process load of whole device.
Further, for reducing the floor space of equipment, improve space availability ratio, described dissolving be arranged on described every
Oil sump and described reactor bottom.
As preferably, tapered bottom described air flotation zone, bottom section, described air flotation zone size is maximum.This kind of structure is not only
Increase the volume bottom air flotation zone, and beneficially being fully contacted of oily waste water and dissolving vent, improve air supporting and imitate
Rate.
Beneficial effect: the application plant area area is little, space availability ratio is high, through oil skimming, dosing reaction, air supporting, two
The oil that the processes such as step precipitation can efficiently be removed in oily waste water divides.
Accompanying drawing explanation
The present invention is further detailed explanation with detailed description of the invention below in conjunction with the accompanying drawings.
Fig. 1 be the application device top view (wherein the first inclined tube filler, the first sludge bucket, the second inclined tube filler to
Go out)；
Fig. 2 is the application device internal structure schematic diagram.
Wherein: 1. oil interceptor, 11. oil skimmers, 2. reactor, 21. agitating devices, 3. air flotation zone, 4. settling zone, 41.
One inclined tube filler, 42. first sludge buckets, 43. deflection plates, 44. Slag Scraping Devices, 45. dirt colleceting areas, 5. clear water zone, 51. water outlet regulations
Device, 6. settling section, 61. second inclined tube fillers, the 62, second sludge bucket, 63. overflow launders, 64. communicating pipes, 65. intermediate pools, 66. rows
Water pipe, 67. air tubes, 7. dissolving, 71. release heads, 72. air compressor machines, 73, reflux pump, 8. sludge outlet.
Detailed description of the invention
Embodiment
As illustrated in fig. 1 and 2, a kind of oily waste water integrated treatment unit, including the oil interceptor 1 set gradually, reactor
2, contact area, clear water zone 5 and settling section 6, passes through baffle interval between described contact area, clear water zone 5 and settling section 6；Described every
It is provided with oil skimmer 11 in oil sump 1, in described reactor 2, agitating device 21 is set；
Described contact area includes air flotation zone 3 and settling zone 4, and described air flotation zone 3 one upper lateral part is with described settling zone 4 even
Logical, it is provided with the release head 71 connected with dissolving 7 bottom described air flotation zone 3, described reactor 2 is the most described by pipeline communication
Bottom air flotation zone 3, tapered bottom described air flotation zone 3, and bottom section, air flotation zone 3 size is maximum；Top, described settling zone 4 sets
It is equipped with Slag Scraping Device 44, in the middle part of it, is provided with the first inclined tube filler 41, bottom it, be provided with the first tapered sludge bucket 42, described
Top, contact area be provided with dirt colleceting area 45, described dirt colleceting area 45 near side, described air flotation zone 3 arrange；Described settling zone 4 one
Side bottom connects with described clear water zone 5, and specifically, bottom described settling zone 4, the side near described clear water zone 5 is provided with folding
Stream plate 43, is obliquely installed towards described clear water zone 5 bottom described deflection plate 43；
Top, described clear water zone 5 connects with described settling section 6, is provided with out water regulator 51, institute in described clear water zone 5
State out water regulator 51 include adjusting rod and be arranged on the block bottom described adjusting rod, described block and side, described clear water zone 5
Wall slipper seal is arranged, and described block moves up and down in described clear water zone 5 thus controls the liquid level in clear water zone 5；Described clear
It is provided with the second inclined tube filler 61 in the middle part of clear district 6, bottom it, is provided with the second tapered sludge bucket 62.Described contact area and
The sludge outlet 8 that the mud at by the first sludge bucket 42 and the second sludge bucket 62 is discharged it is provided with bottom settling section 6.
Described dissolving 7 is arranged on bottom described oil interceptor 1 and described reactor 2, and described dissolving 7 connects to be had with outward
The air compressor machine 72 of boundary's air communication and the reflux pump 73 connected with clear water zone 5.
Further, described settling section 6 top is provided with overflow launder 63, and described second sludge bucket 62 is internal to be tied for hollow
Structure, its hollow structure forms intermediate pool 65, and described overflow launder 63 passes through to connect with described intermediate pool 65 communicating pipe 64, described centre
Pond 65 is in communication with the outside by air tube 67, and described intermediate pool 65 is provided with drain pipe 66.
Operation principle is as follows, is passed through by oil-polluted water in oil interceptor 1, is passed through reactor 2 after oil skimmer 11 oil skimming, to
Add the medicaments such as flocculant such as in reactor 2 to react, at the release head 71 in being delivered to air flotation zone 3 through pipeline, release head
Gas in 71 release dissolvings 7 carries out air supporting operation, and slag body swims in top, settling zone 4, and Slag Scraping Device 44 can be by floating slag
Body is scraped to dirt colleceting area 45；Waste water through first inclined tube filler 41 precipitation after, sludge settling groove between the first sludge bucket 42
In, sludge bucket makes bottom precipitation tend to tranquil, does not flows, and the clear water after precipitation, in deflection plate 43 arrives clear water zone 5, is rolled over
Stream plate 43 can prevent precipitation from entering clear water zone 5 further；Water in clear water zone 5 drains into depositing reservoir, through the second inclined tube filler 61
Precipitating, precipitation concentrates in the groove between the second sludge bucket 62, and the second inclined tube filler 61 top is clear water, clean water overflow
To overflow launder 63, and by storing in being passed through intermediate pool 65 communicating pipe 64 or further continuance lifting, conveying operations；Settling zone
4 and the sludge settling of settling section 6 periodically discharge through sludge outlet 8.Regulated by the water outlet in regulation clear water zone 5 in the process
Device 51, according to the runoff investigation of whole device, can regulate the water level of settling zone 4, so that Slag Scraping Device 44 normally works.
Should be appreciated that specific embodiment described above is only used for explaining the present invention, be not intended to limit the present invention.By
What the spirit of the present invention was extended out obviously changes or changes among still in protection scope of the present invention.
Claims (10)
1. an oily waste water integrated treatment unit, it is characterised in that: include oil interceptor (1), the reactor set gradually
(2), contact area, clear water zone (5) and settling section (6), by between dividing plate between described contact area, clear water zone (5) and settling section (6)
Every, described contact area includes air flotation zone (3) and settling zone (4), described air flotation zone (3) upper lateral part and described settling zone (4)
Connection, described air flotation zone (3) bottom is provided with the release head (71) connected with dissolving (7), and described reactor (2) passes through pipeline
It is communicated to bottom, described air flotation zone (3)；Described settling zone (4) top is provided with Slag Scraping Device (44), is provided with first oblique in the middle part of it
Tube packing (41), is provided with tapered the first sludge bucket (42) bottom it；Described settling zone (4) side bottom and described clear water
District (5) connects, and described clear water zone (5) top connects with described settling section (6)；It is oblique that described settling section (6) middle part is provided with second
Tube packing (61), is provided with tapered the second sludge bucket (62) bottom it.
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described oil interceptor sets in (1)
It is equipped with oil skimmer (11), agitating device (21) is set in described reactor (2).
Oily waste water integrated treatment unit the most according to claim 1 and 2, it is characterised in that: on described contact area
Portion is provided with dirt colleceting area (45), and described dirt colleceting area (45) are arranged near described air flotation zone (3) side.
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described contact area and clarification
Bottom, district (6) is provided with sludge outlet (8).
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described (4) end, settling zone
Portion is provided with near the side of described clear water zone (5) bottom deflection plate (43), described deflection plate (43) towards described clear water zone (5)
It is obliquely installed.
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: in described clear water zone (5)
Be provided with out water regulator (51), described in go out water regulator (51) and include adjusting rod and be arranged on the gear bottom described adjusting rod
Block, described block seals with described clear water zone (5) side walls and arranges, and described block moves up and down in described clear water zone (5)
Thus control the liquid level in clear water zone (5).
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described settling section (6) top
Being provided with overflow launder (63), described second sludge bucket (62) is internal is hollow structure, and its hollow structure forms intermediate pool (65), institute
State overflow launder (63) by connect with described intermediate pool (65) communicating pipe (64), described intermediate pool (65) pass through air tube (67) and
Extraneous connection, described intermediate pool (65) is provided with drain pipe (66).
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: also include and described dissolving
(7) air compressor machine (72) connected with outside air connected and the reflux pump (73) connected with clear water zone (5).
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described dissolving (7) sets
Put in described oil interceptor (1) and described reactor (2) bottom.
Oily waste water integrated treatment unit the most according to claim 1, it is characterised in that: described air flotation zone (3) bottom
Tapered, described air flotation zone (3) bottom section size is maximum.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610754239.7A CN106186443A (en) | 2016-08-30 | 2016-08-30 | Oily waste water integrated treatment unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610754239.7A CN106186443A (en) | 2016-08-30 | 2016-08-30 | Oily waste water integrated treatment unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106186443A true CN106186443A (en) | 2016-12-07 |
Family
ID=57527448
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610754239.7A Pending CN106186443A (en) | 2016-08-30 | 2016-08-30 | Oily waste water integrated treatment unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106186443A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106587298A (en) * | 2016-12-13 | 2017-04-26 | 北京中科润金环保工程股份有限公司 | Oil removing and coagulating sedimentation device for oil field waste liquid treatment |
| CN109956523A (en) * | 2017-12-26 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resinon sewage and waste water treatment device |
| CN110052161A (en) * | 2019-04-08 | 2019-07-26 | 湘潭大学 | VOC photocatalysis treatment system |
| CN110585796A (en) * | 2019-08-08 | 2019-12-20 | 山东大学苏州研究院 | Pretreatment device for recycling release agent wastewater |
| CN112573742A (en) * | 2020-12-31 | 2021-03-30 | 杭州天易成环保设备股份有限公司 | Micro-interface oil removal system and control method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203095663U (en) * | 2013-01-28 | 2013-07-31 | 江苏启创环境科技有限公司 | Integrated air floating device |
| CN204918051U (en) * | 2015-08-14 | 2015-12-30 | 潍坊市天源环保科技有限公司 | Air supporting pipe chute all -in -one |
| CN205115091U (en) * | 2015-09-24 | 2016-03-30 | 安徽师范大学 | Air supporting method treatment facility that industrial waste gas administered |
| CN205442867U (en) * | 2016-01-05 | 2016-08-10 | 宜兴市永创环保科技有限公司 | High -efficient air supporting separator |
| CN205999181U (en) * | 2016-08-30 | 2017-03-08 | 江苏国松环境科技开发有限公司 | Oily waste water integrated treatment unit |
-
2016
- 2016-08-30 CN CN201610754239.7A patent/CN106186443A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203095663U (en) * | 2013-01-28 | 2013-07-31 | 江苏启创环境科技有限公司 | Integrated air floating device |
| CN204918051U (en) * | 2015-08-14 | 2015-12-30 | 潍坊市天源环保科技有限公司 | Air supporting pipe chute all -in -one |
| CN205115091U (en) * | 2015-09-24 | 2016-03-30 | 安徽师范大学 | Air supporting method treatment facility that industrial waste gas administered |
| CN205442867U (en) * | 2016-01-05 | 2016-08-10 | 宜兴市永创环保科技有限公司 | High -efficient air supporting separator |
| CN205999181U (en) * | 2016-08-30 | 2017-03-08 | 江苏国松环境科技开发有限公司 | Oily waste water integrated treatment unit |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106587298A (en) * | 2016-12-13 | 2017-04-26 | 北京中科润金环保工程股份有限公司 | Oil removing and coagulating sedimentation device for oil field waste liquid treatment |
| CN109956523A (en) * | 2017-12-26 | 2019-07-02 | 宜兴市兴南复合材料厂有限公司 | Resinon sewage and waste water treatment device |
| CN110052161A (en) * | 2019-04-08 | 2019-07-26 | 湘潭大学 | VOC photocatalysis treatment system |
| CN110585796A (en) * | 2019-08-08 | 2019-12-20 | 山东大学苏州研究院 | Pretreatment device for recycling release agent wastewater |
| CN112573742A (en) * | 2020-12-31 | 2021-03-30 | 杭州天易成环保设备股份有限公司 | Micro-interface oil removal system and control method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106186443A (en) | Oily waste water integrated treatment unit | |
| CN102092816A (en) | Oil slick recovery device | |
| CN209210512U (en) | Industrial oily wastewater water-oil separating oil-isolating device | |
| CN106955507A (en) | Synchronous rotary dynamic defoaming device | |
| CN205999179U (en) | Oil-containing waste water treating device | |
| CN106075965A (en) | Strain ability of swimming to give up muddy water recovery pond | |
| CN102397712B (en) | Mobile oil-water separation device with floating oil absorber | |
| CN205999181U (en) | Oily waste water integrated treatment unit | |
| CN207169113U (en) | A kind of oil water separator | |
| JP5430790B1 (en) | Channel type floating oil recovery device | |
| CN206089268U (en) | Novel oiliness waste water treatment device | |
| CN102153263A (en) | Efficient sludge concentration and dehydration system and dehydration method thereof | |
| CN1299794C (en) | Floating circular current oil receiver and circular current separating method | |
| CN205258184U (en) | Oily wastewater treating device | |
| CN208828041U (en) | Petrochemical industry deck floor drain | |
| CN106630316A (en) | Integrated multiphase-flow treatment device for oil-containing sewage and sewage treatment method | |
| CN206950722U (en) | Synchronous rotary dynamic defoaming device | |
| CN207877308U (en) | A kind of highly integrated air-floating apparatus | |
| CN207391057U (en) | A kind of agglomerated air floatation efficient degreasing equipment | |
| CN110104820A (en) | A kind of oil water separator | |
| CN105986564A (en) | Retaining device for vacuum oil receiving machine | |
| CN212102409U (en) | Oily wastewater treatment device | |
| CN204298104U (en) | Fiberglass oil interceptor | |
| CN204162537U (en) | For the heavy water treating equipment of dense medium speed of underground coal mine | |
| CN109250828A (en) | A kind of integrated glass fiber reinforced plastic oil removal pool device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161207 |
|
| RJ01 | Rejection of invention patent application after publication |