CN205953777U - Integrated form sewage treatment unit - Google Patents
Integrated form sewage treatment unit Download PDFInfo
- Publication number
- CN205953777U CN205953777U CN201620864112.6U CN201620864112U CN205953777U CN 205953777 U CN205953777 U CN 205953777U CN 201620864112 U CN201620864112 U CN 201620864112U CN 205953777 U CN205953777 U CN 205953777U
- Authority
- CN
- China
- Prior art keywords
- sedimentation basin
- sewage treatment
- chamber
- connects
- treatment device
- 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.)
- Expired - Fee Related
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000004062 sedimentation Methods 0.000 claims abstract description 41
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 33
- 239000003814 drug Substances 0.000 claims abstract description 23
- 238000005273 aeration Methods 0.000 claims abstract description 19
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 238000005189 flocculation Methods 0.000 claims abstract description 7
- 230000016615 flocculation Effects 0.000 claims abstract description 7
- 239000010802 sludge Substances 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 7
- 238000006385 ozonation reaction Methods 0.000 claims description 20
- 238000005188 flotation Methods 0.000 claims description 13
- 239000002253 acid Substances 0.000 claims description 10
- 239000002360 explosive Substances 0.000 claims description 9
- 238000009298 carbon filtering Methods 0.000 claims description 8
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 5
- 230000003311 flocculating effect Effects 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 238000013461 design Methods 0.000 abstract description 4
- 238000007726 management method Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000002781 deodorant agent Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 206010038743 Restlessness Diseases 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000002421 anti-septic effect Effects 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model relates to an integrated form sewage treatment unit, including the air supporting pond, sedimentation tank and ozone aerating filter tank, it dissolves the air chamber to be equipped with in the air supporting pond, the separation chamber, scum chamber and clean water basin, dissolve the air chamber, the separation chamber, the scum chamber, the clean water basin connects gradually, the water inlet that dissolves the air chamber passes through pipe connection flocculation medicine system, the delivery port of clean water basin passes through the pipe connection sedimentation tank, be equipped with the swash plate that the slope was arranged in the settling zone of sedimentation tank, the sedimentation tank bottom is equipped with sludge bucket, ozone aerating filter tank is connected through middle water pump to the delivery port of sedimentation tank, be equipped with activated carbon filter layer in the ozone aerating filter tank, activated carbon filter layer below in bottom is equipped with the aeration head in the ozone aerating filter tank, compared with the prior art, the utility model, can effectively get rid of the pollutant among the little pollution domestic sewage in, low riverway water if polluting substances concentration at this within range, also applicable, and the design is succinct, arranges the compactness, the operation management of being convenient for, the low energy consumption is the environmental protection again, gets rid of effectually.
Description
[technical field]
The utility model is related to micro- pollution sanitary sewage (inclusion laundry effluents) Collection utilization technical field, specifically
It is a kind of integrated domestic sewage treatment device.
[background technology]
With the quickening of Urbanization in China, town dweller's quality of life steps up, and the resident living water water yield increases
Greatly, city domestic sewage discharge capacity increases, and the polluter species in sewage is also increasingly various.Directly arrange for reducing municipal sewage
It is rivals in a contest the adverse effect of ecological environment, reduce the burden of municipal sewage plant, improve the comprehensive utilization ratio of water resource, it is right to need
This kind of waste water is processed.Simultaneously as several years ago the unrest row of waste water so that urban river water also receives a certain degree of pollution,
This part water body also needs purified treatment badly.The research of urban sewage treatment process technology in recent years has become as emphasis although each
Item handling process has obtained certain renewal with equipment, but on the whole, processing cost is larger, and disposal ability still suffers from certain
Limit, comprehensive treatment effect is unsatisfactory.
[utility model content]
The purpose of this utility model seeks to solve above-mentioned deficiency and provides a kind of integrated domestic sewage treatment device,
The pollutant in micro- pollution sanitary sewage can effectively be removed, and design succinct, characteristics of compact layout, be easy to operation management, low energy consumption
Environmental protection again, removal effect is good.
Design a kind of integrated domestic sewage treatment device for achieving the above object, including flotation tank 14, sedimentation basin 15 and
Ozonation aerated filter tank 16, is provided with molten air chamber 1, separation chamber 2, scum chamber 3 and clear water reserviors 4, described molten air chamber in described flotation tank 14
1st, separation chamber 2, scum chamber 3, clear water reserviors 4 are sequentially connected, and the water inlet of described molten air chamber 1 is connected with sewage water inlet pipe, described molten
The water inlet of air chamber 1 connects flocculation medicine system 10 by pipeline, and the delivery port of described clear water reserviors 4 connects sedimentation basin by pipeline
15, it is provided with the swash plate 6 being in tilted layout in the settling zone of described sedimentation basin 15, described sedimentation basin 15 bottom is provided with sludge bucket 7, described
The delivery port of sedimentation basin 15 connects ozonation aerated filter tank 16 by middle water pump 17, is provided with activity in described ozonation aerated filter tank 16
Carbon filtration layer 8, is provided with aeration head 9 below the inner bottom part activated carbon filtering layer 8 of described ozonation aerated filter tank 16.
It is provided with PH on-line computing model 5, described sedimentation basin 15 connects acid dosing respectively by pipeline in described sedimentation basin 15
System 11, alkaline medicine system 12.
Described aeration head 9 connects ozone generator 13 by pipeline.
Described aeration head 9 adopts titanium alloy aeration head.
It is provided with adapter, described adapter one end connects to ozonation aerated filter tank 16 at the bottom of pond, institute in described ozonation aerated filter tank 16
State the outlet pipe that the connection of the adapter other end is connected with filtered water tank.
Described sedimentation basin 15 inner swash plate 6 becomes 60 ° with the angle of horizontal plane.
The water inlet of described sedimentation basin 15 is arranged at swash plate below 6, and delivery port is arranged at swash plate more than 6.
Described sedimentation basin 15 pool wall is provided with the perforated pipe for collecting clear water, the tube wall of described perforated pipe offers some
Perforation.
Described flocculation medicine system 10, acid medicine system 11, alkaline medicine system 12 include respectively explosive barrel, agitator and
Chemicals feed pump, inside explosive barrel, described chemicals feed pump connects the dispensing mouth of explosive barrel by pipeline to described agitator.
Described scum chamber 3 bottom connects mud by screw pump 18 and transports outward pipeline, and dissolved air water is passed through in described clear water reserviors 4 bottom
Pump 19 connects molten air chamber 1.
The utility model compared with the existing technology, has the advantage that：
(1) this device mainly includes flotation tank, sedimentation basin, the ozonation aerated filter tank of activated carbon and auxiliary device (blower fan, spiral shell
Bar pump, dissolved air water pump and corresponding medicine system etc.), its characteristics of compact layout, integral device long service life, each process section pair
The clearance of polluter is high, and effluent quality is good；
(2) flotation tank selects shallow air-floatation technique, and shallow air-floatation is a kind of advanced quick air-flotation system, in traditional gas
In floating theoretical foundation, successfully combine " shallow-layer theoretical " and " zero-speed " principle, by well-designed, will condense, air supporting, skimming,
Precipitation, scrape slag and be integrated, and by adding flocculant, go the removal of impurity, become the high-efficiency appliance of purification of water quality；
(3) sedimentation basin is provided with swash plate (pipe) settling zone, and its effect is not only separation of solid and liquid, and it also has the work(adjusting PH
Effect；
(4) aerating filter adopts titanium alloy aeration head, and intensity is high, corrosion-resistant, light weight, long service life, in filter tank with
Activated carbon is filtrate, and activated carbon specific surface area is big, not only good suction-operated, and its own also has catalysed oxidn；
(5) back segment increases aerating filter, not only can reduce COD, BOD content further, and can be used for water body
Decolouring, deodorant, reduction water turbidity, make the removal efficiency of water body entirety pollutant significantly increase, effluent quality strictly reaches
The standard of surface water one-level A；
(6) micro- pollution sanitary sewage (COD can effectively be removed<300mg/L) the pollutant in (inclusion laundry effluents),
If in, low urban river water pollutant concentration within the range, also applicable, and design succinct, be easy to operation management, low energy consumption
Environmental protection again, removal effect is good.
[brief description]
Fig. 1 is structural representation of the present utility model；
In figure：1st, molten air chamber 2, separation chamber 3, scum chamber 4, clear water reserviors 5, PH on-line computing model 6, swash plate 7, mud
Bucket 8, activated carbon filtering layer 9, aeration head 10, flocculation medicine system 11, acid medicine system 12, alkaline medicine system 13,
Ozone generator 14, flotation tank 15, sedimentation basin 16, ozonation aerated filter tank 17, middle water pump 18, screw pump 19, molten gas
Water pump.
[specific embodiment]
Below in conjunction with the accompanying drawings the utility model is made further explained below：
As shown in Figure 1, the utility model includes：Flotation tank 14, sedimentation basin 15 and ozonation aerated filter tank 16, flotation tank 14
Using shallow air-floatation technique, in pond, it is provided with molten air chamber 1, separation chamber 2, scum chamber 3 and clear water reserviors 4, molten air chamber 1, separation chamber 2, floating
Grit chamber 3, clear water reserviors 4 are sequentially connected, and the water inlet of molten air chamber 1 is connected with sewage water inlet pipe, and sewage flows into gas from sewage water inlet pipe
The molten air chamber 1 of floating chamber 14, simultaneously molten air chamber 1 water inlet by pipeline connect flocculation medicine system 10, by flocculate dosing
System 10 adds the impurity in the flocculants such as PAC or PAM, flocculant and sewage in air supporting interior generation bridging, cohesion, Ran Hou
In separation chamber 2, separation of solid and liquid is carried out by gravitational difference, then pass through and scrape slag equipment scum silica frost is skimmed, last clear water flows into clear water reserviors
4, the delivery port of clear water reserviors 4 connects sedimentation basin 15 by pipeline, flows under the influence of gravity into sedimentation basin from the water outlet of flotation tank, sinks
It is provided with the swash plate 6 being in tilted layout, swash plate 6 becomes 60 ° with the angle of horizontal plane, and sedimentation basin 15 pool wall is provided with the settling zone in shallow lake pond 15
For collecting the perforated pipe of clear water, the tube wall of perforated pipe offers some perforation, sedimentation basin 15 bottom is provided with sludge bucket 7, water
Stream flows from bottom to top, and clear water is collected with perforated pipe in pool wall, and sludge accumulation in sludge bucket 7, is collected by discharge pipeline, entered
City planting ductwork, the delivery port of sedimentation basin 15 connects ozonation aerated filter tank 16 by middle water pump 17, sets in ozonation aerated filter tank 16
Active carbon filtration layer 8, is provided with aeration head 9 below the inner bottom part activated carbon filtering layer 8 of ozonation aerated filter tank 16, and aeration head 9 adopts titanium to close
Golden aeration head, aeration head 9 connects ozone generator 13 by pipeline, and ozone generator 13 is as the ozonation aerated system of activated carbon
Source of oxygen, is provided with adapter in ozonation aerated filter tank 16, adapter one end connects to ozonation aerated filter tank 16 at the bottom of pond, and the adapter other end is even
Connect the outlet pipe being connected with filtered water tank, the water outlet of sedimentation basin squeezes into the ozonation aerated filter tank of activated carbon by middle water pump, using spray
The mode drenched, increases the gas liquid interfacial area of ozone and waste water, and sewage flows through activated carbon filtering layer 8 from top to bottom, and water outlet is from the bottom of pond
Adapter is discharged.
Wherein, it is provided with PH on-line computing model 5 in sedimentation basin 15, the pH value being fed back by on-line computing model, quantitatively add acid
It is each a set of that alkali, therefore sedimentation basin 15 connect acid medicine system 11, alkaline medicine system 12 respectively by pipeline, heavy for adjusting
PH in the pond of shallow lake, this flocculation medicine system 10, acid medicine system 11, alkaline medicine system 12 include explosive barrel, agitator respectively
And chemicals feed pump, inside explosive barrel, chemicals feed pump connects the dispensing mouth of explosive barrel by pipeline to agitator；The water inlet of sedimentation basin 15 sets
It is placed in swash plate below 6, delivery port is arranged at swash plate more than 6；Scum chamber 3 bottom connects mud by screw pump 18 and transports outward pipeline,
Clear water reserviors 4 bottom connects molten air chamber 1 by dissolved air water pump 19.
The utility model innovative point is to combine air supporting, aeration filtration and carbon filtration in a set of equipment, and back segment is set up
Certain thickness activated carbon filtering layer is laid, not only can improve reduction COD, BOD content, but also can decolour in aerating filter
Deodorant, reduce water turbidity, simple and compact device, long service life, running cost is low, operational management is simple, and water quality completely may be used
Up to standard.
In the utility model, what flotation tank used is that shallow air-floatation is theoretical, and shallow air-floatation theory is one kind of air-dissolving air-float
Major way, its device collection cohesion, air supporting, skimming, be deposited in one.Sewage flows into molten air chamber through former pond, simultaneously in shallow-layer
Air supporting sewage inlet pipe mouth adds the flocculant such as PAC, PAM, is sufficiently mixed through flotation tank bottom pipe, and then with air dissolving system
The partly positively charged micro-bubble mixing producing, makes micro-bubble be adsorbed with the pollutant in floccule body, waste water, wadding
Solidifying flco and the pollutant being adsorbed bridging by microbubble carry out rapidly solid-liquid in separation chamber in the presence of buoyancy and zero velocity
Separate, scum silica frost is scraped slag equipment and brought scum chamber into, clear water flows into water-supplying chamber.In shallow air-floatation pond sewage hydraulic detention time short,
Surface loading is high, and pollutants removal rate is high, to the clearance of suspension up to 90%.
In the utility model, in sedimentation basin settling zone, set swash plate (inclined tube), bottom sets sludge bucket, and water inlet is from swash plate (pipe)
Portion is entered, and current flow from bottom to top, and water outlet is collected with perforated pipe in pool wall, and the function of the sedimentation basin in the utility model is except solid
Liquid separates, and also adjusts the effect of PH, and it is each a set of therefore to need to set soda acid medicine system, actually measured according to PH detector in pond
Acid-base value quantitatively add acid or alkali, swash plate (pipe) sedimentation basin removal efficiency is high, and the time of staying is short, and floor space is little.
In the utility model, in aerating filter, set activated carbon filtering layer, bottom sets titanium alloy aeration head, by external source of oxygen
Inwardly lead to ozone from pond bottom and carry out aeration, titanium alloy aeration head light weight, intensity are high, antiseptic property is good, long service life.
The utility model is not limited by above-mentioned embodiment, other any real without departing from spirit of the present utility model
Matter and the change made under principle, modification, replacement, combine, simplify, all should be equivalent substitute mode, be included in this practicality
Within new protection domain.
Claims (10)
1. a kind of integrated domestic sewage treatment device it is characterised in that：Expose including flotation tank (14), sedimentation basin (15) and ozone
Air filter pond (16), is provided with molten air chamber (1), separation chamber (2), scum chamber (3) and clear water reserviors (4) in described flotation tank (14), described
Molten air chamber (1), separation chamber (2), scum chamber (3), clear water reserviors (4) are sequentially connected, and the water inlet of described molten air chamber (1) is entered with sewage
Water pipe connects, and the water inlet of described molten air chamber (1) passes through pipeline and connects medicine system (10) of flocculating, the going out of described clear water reserviors (4)
The mouth of a river connects sedimentation basin (15) by pipeline, is provided with the swash plate (6) being in tilted layout in the settling zone of described sedimentation basin (15), described
Sedimentation basin (15) bottom is provided with sludge bucket (7), and the delivery port of described sedimentation basin (15) connects ozone by middle water pump (17) and exposes
Air filter pond (16), is provided with activated carbon filtering layer (8), described ozonation aerated filter tank (16) inner bottom part in described ozonation aerated filter tank (16)
It is provided with aeration head (9) below activated carbon filtering layer (8).
2. integrated domestic sewage treatment device as claimed in claim 1 it is characterised in that：It is provided with described sedimentation basin (15)
PH on-line computing model (5), described sedimentation basin (15) connects acid medicine system (11), alkaline medicine system respectively by pipeline
(12).
3. integrated domestic sewage treatment device as claimed in claim 2 it is characterised in that：Described aeration head (9) passes through pipe
Road connects ozone generator (13).
4. integrated domestic sewage treatment device as claimed in claim 2 or claim 3 it is characterised in that：Described aeration head (9) adopts
Titanium alloy aeration head.
5. integrated domestic sewage treatment device as claimed in claim 4 it is characterised in that：Described ozonation aerated filter tank (16)
Inside it is provided with adapter, described adapter one end connects to ozonation aerated filter tank (16) at the bottom of pond, and the described adapter other end connects and filtered water tank
Connected outlet pipe.
6. integrated domestic sewage treatment device as claimed in claim 5 it is characterised in that：Described sedimentation basin (15) inner swash plate
(6) 60 ° are become with the angle of horizontal plane.
7. integrated domestic sewage treatment device as claimed in claim 6 it is characterised in that：The water inlet of described sedimentation basin (15)
Mouth is arranged at swash plate (6) below, and delivery port is arranged at more than swash plate (6).
8. integrated domestic sewage treatment device as claimed in claim 7 it is characterised in that：Described sedimentation basin (15) pool wall sets
There is the perforated pipe for collecting clear water, the tube wall of described perforated pipe offers some perforation.
9. integrated domestic sewage treatment device as claimed in claim 8 it is characterised in that：Described flocculation medicine system
(10), acid medicine system (11), alkaline medicine system (12) include explosive barrel, agitator and chemicals feed pump, described agitator respectively
Inside explosive barrel, described chemicals feed pump connects the dispensing mouth of explosive barrel by pipeline.
10. integrated domestic sewage treatment device as claimed in claim 9 it is characterised in that：Described scum chamber (3) bottom leads to
Cross screw pump (18) and connect mud outward transport pipeline, described clear water reserviors (4) bottom connects molten air chamber (1) by dissolved air water pump (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620864112.6U CN205953777U (en) | 2016-08-11 | 2016-08-11 | Integrated form sewage treatment unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620864112.6U CN205953777U (en) | 2016-08-11 | 2016-08-11 | Integrated form sewage treatment unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205953777U true CN205953777U (en) | 2017-02-15 |
Family
ID=57974536
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620864112.6U Expired - Fee Related CN205953777U (en) | 2016-08-11 | 2016-08-11 | Integrated form sewage treatment unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205953777U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055954A (en) * | 2017-03-30 | 2017-08-18 | 山东建筑大学 | A kind of charcoal circular form pool water cleaning systems and method |
| CN107892457A (en) * | 2017-12-19 | 2018-04-10 | 上海城市水资源开发利用国家工程中心有限公司 | A kind of sludge microbubble ozone stable device and method |
| CN109603214A (en) * | 2019-01-02 | 2019-04-12 | 国电银河水务股份有限公司 | A sloping plate sedimentation tank for sewage treatment |
| CN110563192A (en) * | 2019-08-05 | 2019-12-13 | 周有 | Aerobic environment multi-effect purification field system for refractory organic matters |
| CN110835184A (en) * | 2019-11-27 | 2020-02-25 | 南通汇佰川工程技术有限公司 | Portable garbage transfer station sewage treatment and recycling system and method |
| CN113912216A (en) * | 2021-11-05 | 2022-01-11 | 深圳市束喜环境科技有限公司 | Sewage treatment equipment and method |
-
2016
- 2016-08-11 CN CN201620864112.6U patent/CN205953777U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107055954A (en) * | 2017-03-30 | 2017-08-18 | 山东建筑大学 | A kind of charcoal circular form pool water cleaning systems and method |
| CN107055954B (en) * | 2017-03-30 | 2020-10-09 | 山东建筑大学 | Biochar circulation type copolymerization air flotation tank water purification system and method |
| CN107892457A (en) * | 2017-12-19 | 2018-04-10 | 上海城市水资源开发利用国家工程中心有限公司 | A kind of sludge microbubble ozone stable device and method |
| CN107892457B (en) * | 2017-12-19 | 2023-06-09 | 上海城市水资源开发利用国家工程中心有限公司 | A sludge microbubble ozone stabilization device and method |
| CN109603214A (en) * | 2019-01-02 | 2019-04-12 | 国电银河水务股份有限公司 | A sloping plate sedimentation tank for sewage treatment |
| CN110563192A (en) * | 2019-08-05 | 2019-12-13 | 周有 | Aerobic environment multi-effect purification field system for refractory organic matters |
| CN110835184A (en) * | 2019-11-27 | 2020-02-25 | 南通汇佰川工程技术有限公司 | Portable garbage transfer station sewage treatment and recycling system and method |
| CN113912216A (en) * | 2021-11-05 | 2022-01-11 | 深圳市束喜环境科技有限公司 | Sewage treatment equipment and method |
| CN113912216B (en) * | 2021-11-05 | 2023-09-01 | 深圳市束喜环境科技有限公司 | Sewage treatment equipment and method |
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Legal Events
| Date | Code | Title | Description |
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