CN208200689U - A kind of industrial wastewater advanced oxidation integrated apparatus - Google Patents
A kind of industrial wastewater advanced oxidation integrated apparatus Download PDFInfo
- Publication number
- CN208200689U CN208200689U CN201820508890.0U CN201820508890U CN208200689U CN 208200689 U CN208200689 U CN 208200689U CN 201820508890 U CN201820508890 U CN 201820508890U CN 208200689 U CN208200689 U CN 208200689U
- Authority
- CN
- China
- Prior art keywords
- wall
- reaction pond
- sedimentation basin
- industrial wastewater
- oxidation reaction
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of industrial wastewater advanced oxidation integrated apparatus, including shell, left end in the housing chamber is equipped with intake pool, the right side of the intake pool outer wall is equipped with sedimentation basin, the right side of the sedimentation basin outer wall is equipped with oxidation reaction pond, the lower end of the driving motor is rotatably connected to shaft, the shaft protrudes into the inside in oxidation reaction pond, the outer surface of the shaft is equipped at intervals with stirring rod, the right side of the driving motor is equipped with feeding opening, oxidation reaction pond inner wall upper end is protruded into the lower end of the feeding opening, the lower end of the feeding opening is communicated with medicine-introducing pipe, the right side of oxidation reaction pond outer wall is equipped with biomembrane reaction pond, the right side of the biomembrane reaction pond outer wall is equipped with sterilization pool, the utility model relates to industrial wastewater advanced oxidation integrated technique fields.The industrial wastewater advanced oxidation integrated apparatus has achieved the purpose that structure is simple, convenient to overhaul, good sewage processing effect, has improved the treatment effeciency of trade effluent.
Description
Technical field
The utility model relates to industrial wastewater advanced oxidation integrated technique field, specially a kind of advanced oxygen of industrial wastewater
Change integrated apparatus.
Background technique
With the high speed development of China's industrialization and urbanization process, the discharge amount of industrial wastewater is more and more, Industry Waste
Often containing harmful substances such as plurality of heavy metal ion, inorganic compound and organic compounds in water, such as Cr, Ni, phosphate, ammonia nitrogen
Compound, organic acid etc., if processing is not up to standard, these substances enter environment and inherently generate extensively to ecological environment and the mankind
General and serious harm, or even by food chain, breathing or directly the path that contacts is enriched in vivo, to biology and
Human health constitutes a threat to, and gene mutation is even caused when serious or induces cancer, traditional biochemical method is difficult to handle
These hardly degraded organic substances.High-level oxidation technology is one of processing most promising method of organic wastewater with difficult degradation thereby, it
It has been increasingly becoming the hot subject of various countries' water treatment technology research.
Ferrous sulfate and hydrogen peroxide mix reagent are a kind of widely applied methods in high-level oxidation technology, pass through sulfuric acid
Ferrous and hydrogen peroxide mixing generates hydroxyl, the Fe being added in water treatment facilities2+Best ratio is controlled with hydrogen peroxide
Example, since the water quality of waste water changes constantly, so ratio needs the moment to adjust in actual motion, is extremely difficult to ideal
Desired effect.The effect of existing industrial wastewater advanced oxidation integrated apparatus sewage treatment is poor, moreover, existing industry
The structure of waste water advanced oxidization integrated apparatus is all more complex, and manufacturing cost is higher, and when failure is inconvenient to overhaul, maintenance at
This is higher.
Utility model content
(1) the technical issues of solving
In view of the deficiencies of the prior art, the utility model provides a kind of industrial wastewater advanced oxidation integrated apparatus, solution
Having determined, structure is complicated, inconvenience is overhauled, the problem of wastewater treatment efficiency difference.
(2) technical solution
In order to achieve the above object, the utility model is achieved by the following technical programs: a kind of advanced oxygen of industrial wastewater
Change integrated apparatus, including shell, the left end in the housing chamber is provided with intake pool, the right side setting of the intake pool outer wall
There is sedimentation basin, the lower end on the left of the sedimentation basin is connected to intake pool, and the bottom end of the sedimentation basin inner wall is fixedly connected with filtering
Plate, the upper end of the filter plate are provided with coarse rack net, the left and right ends of the coarse rack net and the fixed company of the inner wall of sedimentation basin
It connects, the upper end of the coarse rack net is provided with fine fack net, and the left and right ends of the fine fack net and the inner wall of sedimentation basin are fixed
It connects, is provided with oxidation reaction pond on the right side of the sedimentation basin outer wall, the upper end on the left of the oxidation reaction pond and sedimentation basin connect
Logical, the position of the oxidation reaction pond outer wall upper surface middle part is provided with driving motor, and the lower end of the driving motor, which rotates, to be connected
It is connected to shaft, the shaft protrudes into the inside in oxidation reaction pond, and the outer surface of the shaft is arranged at intervals with stirring rod, the drive
It is provided with feeding opening on the right side of dynamic motor, oxidation reaction pond inner wall upper end is protruded into the lower end of the feeding opening, the feeding opening
Lower end is communicated with medicine-introducing pipe, and the right side of the medicine-introducing pipe outer wall is fixedly connected by fixed bracket with oxidation reaction pond inner wall, institute
It states and is provided with biomembrane reaction pond on the right side of the outer wall of oxidation reaction pond, lower end and oxidation reaction on the left of the biomembrane reaction pond
Pond connection, the inner wall at left and right sides of the biomembrane reaction pond are symmetrically arranged with the first fixed plate, between first fixed plate
The position of lower end is provided with MBR membrane reactor, and the upper end of the MBR membrane reactor is provided with reverse osmosis membrane, and the biomembrane is anti-
It answers and is provided with sterilization pool on the right side of the outer wall of pond, the upper end on the left of the sterilization pool is connected to biomembrane reaction pond, the sterilization pool
The inner wall of the left and right sides is symmetrically arranged with the second fixed plate, is provided with taste removal layer between second fixed plate.
Preferably, the inside of the filter plate is uniformly provided with inclined hole, and the lower end on the left of the housing exterior walls is provided with
The right end of one aeration pump, first aeration pump is connected to by tracheae with sedimentation basin.
Preferably, the inside of the stirring rod is uniformly provided with through-hole, and the stirring rod symmetrically and evenly has nine.
Preferably, the bottom of the housing exterior walls is provided with sludge collecting tank, the sludge collecting tank outer wall lower end middle part
Position be provided with the second aeration pump, the upper end of second aeration pump is connected to by tracheae with biomembrane reaction pond.
Preferably, the inside of the taste removal layer is uniformly filled with active fruit shell carbon, and the upper and lower ends of the taste removal layer are all provided with
It is equipped with ultrafiltration membrane.
Preferably, the upper end on the left of the intake pool outer wall is communicated with water inlet pipe, the right side connection of the sterilization pool outer wall
There is discharge bay, the upper end on the right side of the discharge bay outer wall is communicated with outlet pipe, and the left and right sides of the housing exterior walls upper surface is right
Title is provided with access hole.
(3) beneficial effect
The utility model provides a kind of industrial wastewater advanced oxidation integrated apparatus.Have it is following the utility model has the advantages that
(1), the industrial wastewater advanced oxidation integrated apparatus, the left end in housing chamber are provided with intake pool, outside intake pool
It is provided with sedimentation basin on the right side of wall, oxidation reaction pond is provided on the right side of sedimentation basin outer wall, is set on the right side of the outer wall of oxidation reaction pond
It is equipped with biomembrane reaction pond, sterilization pool is provided on the right side of biomembrane reaction pond outer wall, is communicated with out on the right side of sterilization pool outer wall
Pond, the upper end on the left of intake pool outer wall are communicated with water inlet pipe, and the upper end on the right side of discharge bay outer wall is communicated with outlet pipe, structure letter
Single easy to install, cost is relatively low, and housing exterior walls are symmetrically arranged with access hole at left and right sides of upper surface, can be overhauled, be reached in time
The purpose that structure is simple, convenient to overhaul has been arrived, maintenance cost is reduced.
(2), the industrial wastewater advanced oxidation integrated apparatus, trade effluent enter the intracorporal water inlet of shell by water inlet pipe
Pond enters in sedimentation basin by intake pool, the first aeration pump is opened, when industrial wastewater passes through filter plate, under the action of inclined hole
Sludge settling is fallen in waste water in precipitating bottom of pond portion, sludge by sludge collecting tank centralized collection, coarse rack net and fine fack net filtration
Sundries and floccule, subsequently into hydrogen peroxide agent in oxidation reaction pond, is added into feeding opening, hydrogen peroxide is by leading
Pencil enters in oxidation reaction pond, and medicine-introducing pipe prevents the sundries in waste water from directly contacting with feeding opening, blocks feeding opening, opens and drives
Motor is moved, through-hole is offered inside stirring rod, is sufficiently mixed waste water with hydrogen peroxide agent, hydrogen peroxide can handle a variety of contain
The waste water of toxic and odorous compound and the waste water of sulfur compound, cyanide, phenol etc., the slight sterilizing of hydrogen peroxide
Performance can also selectively kill certain microorganisms for causing activated sludge bulking, and normally give birth to in activated sludge process
Object does not generate adverse effect, and the waste water after oxidation enters in biomembrane reaction pond, opens the second aeration pump, makes tap water and MBR
Membrane reactor sufficiently reacts, MBR membrane reactor because of its effective crown_interception, can the longer microorganism of retention periods, it can be achieved that
To deep purification of waste water, the membrane aperture of reverse osmosis membrane is very small, dissolved salts, the colloid, micro- life that can be effectively removed in water
Object, organic matter etc., finally enter sterilization pool, by the filtering of ultrafiltration membrane and active carbon, remove remaining bacterium and peculiar smell, reach
The purpose of good sewage processing effect, improves the treatment effeciency of trade effluent.
Detailed description of the invention
Fig. 1 is the industrial wastewater advanced oxidation integrated apparatus structural schematic diagram of the utility model；
Fig. 2 is the oxidation reaction pool structure schematic diagram of the utility model；
Fig. 3 is the biomembrane reaction pond structural schematic diagram of the utility model；
Fig. 4 is the sterilization pool structural schematic diagram of the utility model.
In figure: 1 shell, 2 intake pools, 3 sedimentation basins, 4 filter plates, 5 coarse rack nets, 6 fine fack nets, 7 oxidation reaction ponds, 8
Driving motor, 9 shafts, 10 stirring rods, 11 feeding openings, 12 medicine-introducing pipes, 13 biomembrane reaction ponds, 14 first fixed plates, 15MBR film
Reactor, 16 reverse osmosis membranes, 17 sterilization pools, 18 second fixed plates, 19 taste removal layers, 20 first aeration pumps, 21 sludge collecting tanks, 22
Second aeration pump, 23 ultrafiltration membranes, 24 water inlet pipes, 25 discharge bays, 26 outlet pipes, 27 access holes.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1-4 is please referred to, the utility model provides a kind of technical solution: a kind of industrial wastewater advanced oxidation integrally makeup
It sets, including shell 1, the intracavitary left end of shell 1 is provided with intake pool 2, and sedimentation basin 3 is provided on the right side of 2 outer wall of intake pool, precipitates
The lower end in 3 left side of pond is connected to intake pool 2, and the bottom end of 3 inner wall of sedimentation basin is fixedly connected with filter plate 4, and the upper end of filter plate 4 is set
It is equipped with coarse rack net 5, the left and right ends of coarse rack net 5 are fixedly connected with the inner wall of sedimentation basin 3, the upper end setting of coarse rack net 5
There is fine fack net 6, the left and right ends of fine fack net 6 are fixedly connected with the inner wall of sedimentation basin 3, the right side setting of 3 outer wall of sedimentation basin
There is oxidation reaction tank 7, the upper end in 7 left side of oxidation reaction pond is connected to sedimentation basin 3,7 outer wall upper surface middle part of oxidation reaction pond
Position is provided with driving motor 8, and the lower end of driving motor 8 is rotatably connected to shaft 9, and shaft 9 protrudes into the interior of oxidation reaction pond 7
Portion, the outer surface of shaft 9 are arranged at intervals with stirring rod 10, and the right side of driving motor 8 is provided with feeding opening 11, under feeding opening 11
7 inner wall upper end of oxidation reaction pond is protruded at end, and the lower end of feeding opening 11 is communicated with medicine-introducing pipe 12, passes through on the right side of 12 outer wall of medicine-introducing pipe
Fixed bracket is fixedly connected with 7 inner wall of oxidation reaction pond, is provided with biomembrane reaction pond 13 on the right side of 7 outer wall of oxidation reaction pond,
The lower end in 13 left side of biomembrane reaction pond is connected to oxidation reaction pond 7, and the inner wall of 13 left and right sides of biomembrane reaction pond is symmetrically set
It is equipped with the first fixed plate 14, the position of lower end is provided with MBR membrane reactor 15, MBR membrane reactor 15 between the first fixed plate 14
Upper end be provided with reverse osmosis membrane 16, be provided with sterilization pool 17 on the right side of 13 outer wall of biomembrane reaction pond, 17 left side of sterilization pool
Upper end is connected to biomembrane reaction pond 13, and the inner wall of 17 left and right sides of sterilization pool is symmetrically arranged with the second fixed plate 18, and second is solid
Taste removal layer 19 is provided between fixed board 18.
The inside of filter plate 4 is uniformly provided with inclined hole, and the lower end on the left of 1 outer wall of shell is provided with the first aeration pump 20, the
The right end of one aeration pump 20 is connected to by tracheae with sedimentation basin 3.
The inside of stirring rod 10 is uniformly provided with through-hole, and stirring rod 10 symmetrically and evenly has nine.
The bottom of 1 outer wall of shell is provided with sludge collecting tank 21, the position setting in the middle part of 21 outer wall lower end of sludge collecting tank
There is the second aeration pump 22, the upper end of the second aeration pump 22 is connected to by tracheae with biomembrane reaction pond 13.
The inside of taste removal layer 19 is uniformly filled with active fruit shell carbon, and the upper and lower ends of taste removal layer 27 are provided with ultrafiltration membrane
23。
Upper end on the left of 2 outer wall of intake pool is communicated with water inlet pipe 24, is communicated with discharge bay 25 on the right side of 17 outer wall of sterilization pool,
Upper end on the right side of 25 outer wall of discharge bay is communicated with outlet pipe 26, and shell is symmetrically arranged with maintenance at left and right sides of 1 outer wall upper surface
Mouth 27.
In use, trade effluent enters the intake pool 2 in shell 1 by water inlet pipe 24, enter sedimentation basin by intake pool 2
In 3, the first aeration pump 20 is opened, when industrial wastewater passes through filter plate 4, sludge settling is at 3 bottom of sedimentation basin under the action of inclined hole
Portion, sludge filter out sundries and floccule in waste water by 21 centralized collection of sludge collecting tank, coarse rack net 5 and fine fack net 6,
Subsequently into hydrogen peroxide agent in oxidation reaction pond 7, is added into feeding opening 11, hydrogen peroxide enters oxygen by medicine-introducing pipe 12
Change in reaction tank 7, medicine-introducing pipe 12 prevents the sundries in waste water from directly contacting with feeding opening 11, blocks feeding opening 11, opens driving
Motor 8 offers through-hole inside stirring rod 10, is sufficiently mixed waste water with hydrogen peroxide agent, hydrogen peroxide can handle a variety of
The waste water of waste water and sulfur compound, cyanide, phenol etc. containing toxic and odorous compound, hydrogen peroxide slightly go out
Bacterium performance can also selectively kill certain microorganisms for causing activated sludge bulking, and to normal in activated sludge process
Biology does not generate adverse effect, and the waste water after oxidation enters in biomembrane reaction pond 13, opens the second aeration pump 22, makes tap water
It is sufficiently reacted with MBR membrane reactor 15, MBR membrane reactor 15, can the longer micro- life of retention periods because of its effective crown_interception
For object, it can be achieved that deep purification of waste water, the membrane aperture of reverse osmosis membrane 16 is very small, the dissolving salt that can be effectively removed in water
Class, colloid, microorganism, organic matter etc. finally enter sterilization pool 17, by the filtering of ultrafiltration membrane 23 and active carbon, removal residual
Bacterium and peculiar smell.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.In the absence of more restrictions.By sentence " element limited including one ..., it is not excluded that
There is also other identical elements in the process, method, article or apparatus that includes the element ".
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of industrial wastewater advanced oxidation integrated apparatus, including shell (1), it is characterised in that: the shell (1) is intracavitary
Left end is provided with intake pool (2), is provided with sedimentation basin (3) on the right side of intake pool (2) outer wall, on the left of the sedimentation basin (3)
Lower end be connected to intake pool (2), the bottom end of sedimentation basin (3) inner wall is fixedly connected with filter plate (4), the filter plate
(4) upper end is provided with coarse rack net (5), the left and right ends of the coarse rack net (5) and the fixed company of the inner wall of sedimentation basin (3)
It connects, the upper end of the coarse rack net (5) is provided with fine fack net (6), the left and right ends of the fine fack net (6) and sedimentation basin
(3) inner wall is fixedly connected, and is provided with oxidation reaction pond (7) on the right side of sedimentation basin (3) outer wall, the oxidation reaction pond
(7) upper end on the left of is connected to sedimentation basin (3), and the position of oxidation reaction pond (7) the outer wall upper surface middle part is provided with driving
The lower end of motor (8), the driving motor (8) is rotatably connected to shaft (9), and the shaft (9) protrudes into oxidation reaction pond (7)
The outer surface of inside, the shaft (9) is arranged at intervals with stirring rod (10), is provided on the right side of the driving motor (8) into medicine
Oxidation reaction pond (7) inner wall upper end, the lower end connection of the feeding opening (11) are protruded into mouth (11), the lower end of the feeding opening (11)
Having medicine-introducing pipe (12), the right side of medicine-introducing pipe (12) outer wall is fixedly connected by fixed bracket with oxidation reaction pond (7) inner wall,
It is provided with biomembrane reaction pond (13) on the right side of oxidation reaction pond (7) outer wall, on the left of the biomembrane reaction pond (13)
Lower end is connected to oxidation reaction pond (7), and it is fixed that the inner wall at left and right sides of the biomembrane reaction pond (13) is symmetrically arranged with first
Plate (14), the position of lower end is provided with MBR membrane reactor (15) between first fixed plate (14), the MBR membrane reactor
(15) upper end is provided with reverse osmosis membrane (16), is provided with sterilization pool (17) on the right side of biomembrane reaction pond (13) outer wall,
Upper end on the left of the sterilization pool (17) is connected to biomembrane reaction pond (13), the inner wall pair at left and right sides of the sterilization pool (17)
Title is provided with the second fixed plate (18), is provided with taste removal layer (19) between second fixed plate (18).
2. a kind of industrial wastewater advanced oxidation integrated apparatus according to claim 1, it is characterised in that: the filter plate
(4) inside is uniformly provided with inclined hole, and the lower end on the left of shell (1) outer wall is provided with the first aeration pump (20), and described
The right end of one aeration pump (20) is connected to by tracheae with sedimentation basin (3).
3. a kind of industrial wastewater advanced oxidation integrated apparatus according to claim 1, it is characterised in that: the stirring rod
(10) inside is uniformly provided with through-hole, and the stirring rod (10) symmetrically and evenly has nine.
4. a kind of industrial wastewater advanced oxidation integrated apparatus according to claim 1, it is characterised in that: the shell (1)
The bottom of outer wall is provided with sludge collecting tank (21), and the position in the middle part of sludge collecting tank (21) the outer wall lower end is provided with second
The upper end of aeration pump (22), second aeration pump (22) is connected to by tracheae with biomembrane reaction pond (13).
5. a kind of industrial wastewater advanced oxidation integrated apparatus according to claim 1, it is characterised in that: the taste removal layer
(19) inside is uniformly filled with active fruit shell carbon, and the upper and lower ends of the taste removal layer (19) are provided with ultrafiltration membrane (23).
6. a kind of industrial wastewater advanced oxidation integrated apparatus according to claim 1, it is characterised in that: the intake pool
(2) upper end on the left of outer wall is communicated with water inlet pipe (24), is communicated with discharge bay (25), institute on the right side of sterilization pool (17) outer wall
It states the upper end on the right side of discharge bay (25) outer wall to be communicated with outlet pipe (26), the left and right sides of shell (1) the outer wall upper surface is right
Title is provided with access hole (27).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820508890.0U CN208200689U (en) | 2018-04-11 | 2018-04-11 | A kind of industrial wastewater advanced oxidation integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820508890.0U CN208200689U (en) | 2018-04-11 | 2018-04-11 | A kind of industrial wastewater advanced oxidation integrated apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208200689U true CN208200689U (en) | 2018-12-07 |
Family
ID=64526144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820508890.0U Expired - Fee Related CN208200689U (en) | 2018-04-11 | 2018-04-11 | A kind of industrial wastewater advanced oxidation integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208200689U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775932A (en) * | 2019-02-27 | 2019-05-21 | 湖南水之源环保科技工程有限公司 | A kind of sewage disposal system |
| CN109952989A (en) * | 2019-03-04 | 2019-07-02 | 浙江大学 | The artificial sinking device of tidal range formula |
| CN110342675A (en) * | 2019-05-17 | 2019-10-18 | 重庆迪盈精密电子科技有限公司 | A kind of environment-protecting industrial wastewater treatment equipment |
| CN110697945A (en) * | 2019-11-22 | 2020-01-17 | 湖南金益环保股份有限公司 | Industrial sewage is desulfurization oxidation pond for secondary treatment based on environmental emission reduction |
| CN112939290A (en) * | 2021-04-20 | 2021-06-11 | 四川省太易净科技有限公司 | Advanced oxidation reactor for industrial sewage treatment |
-
2018
- 2018-04-11 CN CN201820508890.0U patent/CN208200689U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775932A (en) * | 2019-02-27 | 2019-05-21 | 湖南水之源环保科技工程有限公司 | A kind of sewage disposal system |
| CN109952989A (en) * | 2019-03-04 | 2019-07-02 | 浙江大学 | The artificial sinking device of tidal range formula |
| CN109952989B (en) * | 2019-03-04 | 2021-03-09 | 浙江大学 | Tidal-difference type artificial down-flow device |
| CN110342675A (en) * | 2019-05-17 | 2019-10-18 | 重庆迪盈精密电子科技有限公司 | A kind of environment-protecting industrial wastewater treatment equipment |
| CN110697945A (en) * | 2019-11-22 | 2020-01-17 | 湖南金益环保股份有限公司 | Industrial sewage is desulfurization oxidation pond for secondary treatment based on environmental emission reduction |
| CN112939290A (en) * | 2021-04-20 | 2021-06-11 | 四川省太易净科技有限公司 | Advanced oxidation reactor for industrial sewage treatment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208200689U (en) | A kind of industrial wastewater advanced oxidation integrated apparatus | |
| CN106045235B (en) | A kind for the treatment of process of high-concentration hardly-degradable wastewater from chemical industry | |
| CN105481174A (en) | Wastewater treatment system in rubber and synthetic plastic industry | |
| CN208471815U (en) | A kind of high-concentration sewage treatment system of AO technique and Fenton system support | |
| CN213112948U (en) | Integrated circulating culture system | |
| CN102249491A (en) | Deep treatment device and process for secondary treatment effluent of urban sewage plant | |
| CN101591121B (en) | Method for treating xanthate wastewater through combination of film biodegradation and hydrogen peroxide oxidation | |
| CN107555600A (en) | A kind of sewage disposal system | |
| CN106673257A (en) | Micropolluted raw water treatment integrated plant | |
| CN105152479B (en) | Modified particles activated carbon couples membrane bioreactor and heavy metal-containing wastewater treatment method | |
| CN209853950U (en) | A sewage treatment plant for circuit board workshop | |
| CN209537234U (en) | A kind of integrated industrial waste water treatment system | |
| CN206273800U (en) | A kind of biofilm sewage treatment device | |
| CN212687845U (en) | Pharmaceutical wastewater comprehensive treatment device | |
| CN204897577U (en) | Mix to congeal and handle and membrane separation combination effluent disposal system | |
| CN207811366U (en) | A kind of sewage disposal system | |
| CN102690022B (en) | Upflow microbial reactor processing technology for manganese-bearing waste water | |
| CN206858369U (en) | A kind of biological sewage treatment device | |
| CN208603832U (en) | A kind of high performance membrane biological reaction pool and sewage disposal system | |
| CN202881063U (en) | Bio-pharmaceutical sewage purification system | |
| CN206467101U (en) | High-concentration hardly-degradable Fine Chemistry Wastewater processing system | |
| CN206940675U (en) | A kind of sanitary wastewater processing equipment | |
| CN109502762A (en) | A kind of sewage disposal device and its workflow of efficient MBBR | |
| CN209226678U (en) | A kind of composite rotating bio-disc processing unit | |
| CN211896566U (en) | Membrane biological wastewater treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181207 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |