CN204342604U - Novel cultivation Sewage treatment systems - Google Patents
Novel cultivation Sewage treatment systems Download PDFInfo
- Publication number
- CN204342604U CN204342604U CN201420736447.0U CN201420736447U CN204342604U CN 204342604 U CN204342604 U CN 204342604U CN 201420736447 U CN201420736447 U CN 201420736447U CN 204342604 U CN204342604 U CN 204342604U
- Authority
- CN
- China
- Prior art keywords
- pond
- tank
- pool
- outlet
- pipeline
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a kind of Novel cultivation Sewage treatment systems, be made up of grating tank, the agitated pool that catchments, solid-liquid separating machine, just heavy hydrolysis acidification pool, IC reactor, one-level anoxic pond, the first sodium carbonate alkali lye pond, one-level Aerobic Pond, intermediate sedimentation pond, secondary anoxic pond, the second sodium carbonate alkali lye pond, secondary Aerobic Pond, medicament pond, dephosphorization settling tank, acidification pool, the oxygen pool of holding concurrently, sterilization pool, the filler of regulating.The collection of the biogas of IC reactor is collected by wet storage holder, the utility model designs this process system according to the feature of feces of farm waste water, good sewage processing effect, final energy qualified discharge, behind SPC-D alkali lye pond, anoxic pond and Aerobic Pond is entered from IC reactor waste water out, be conducive to microbial growth, improve the efficiency of anoxic and aerobic treatment, while sewage disposal, produce biogas.
Description
Technical field
The utility model relates to a kind of Novel cultivation Sewage treatment systems.
Background technology
In recent years; along with the raising of expanding economy and living standards of the people; livestock products demand also constantly increases; facilitate the livestock breeding industry of China towards mass-producing, intensive future development thereupon; according to investigations, current domestic most plant all have employed the mode of dry clear excrement, and the livestock breeding wastewater of generation is mostly rinse the waste water such as colony house; these waste water directly enter or enter river,lake and reservior with rain drop erosion, make water body blackening smelly.Permeate the ground for a long time, the nitrate content in underground water is increased, water quality deterioration, severe contamination plant's surrounding enviroment and underground water, threaten the healthy of resident near plant;
In addition, current useful wet storage holder collects biogas, but existing wet storage holder is generally coordinated by a guide rail and slide block or pulley floating cover is moved up and down, once pulley goes wrong, floating cover can not float, now, tank internal pressure increases, and the consequence brought therefrom dare not be imagined.
Utility model content
For existing problem, the purpose of this utility model is to provide a kind of Novel cultivation Sewage treatment systems.
To achieve these goals, the technical solution of the utility model is: a kind of Novel cultivation Sewage treatment systems, comprise grating tank (1), it is characterized in that: the water outlet of described grating tank (1) is connected with the agitated pool that catchments (2), stirrer (2a) is provided with in the described agitated pool that catchments (2), the water outlet of the described agitated pool that catchments (2) is extracted into solid-liquid separating machine (3) by pump, the liquid exit of described solid-liquid separating machine (3) is connected to just heavy adjustment hydrolysis acidification pool (4) by pipeline, the described just heavy bottom of hydrolysis acidification pool (4) that regulates is provided with sludge pump, the described just heavy liquid exit of hydrolysis acidification pool (4) that regulates is connected with the import of IC reactor (5), air outlet on the upper outlet body of described IC reactor (5) is connected with methane purifying device (61) by pipeline, the outlet of described methane purifying device (61) is connected with wet storage holder (62) by pipeline, the liquid exit of described IC reactor (5) is connected with one-level anoxic pond (7) by pipeline, the outlet of described one-level anoxic pond (7) is connected with the first sodium carbonate alkali lye pond (8), the outlet in described first sodium carbonate alkali lye pond (8) is connected with one-level Aerobic Pond (9), the outlet of described one-level Aerobic Pond (9) is connected with intermediate sedimentation pond (10) by pipeline, the water outlet of described intermediate sedimentation pond (10) is connected with secondary anoxic pond (11) by pipeline, described secondary anoxic pond (11) is connected with the second sodium carbonate alkali lye pond (12) by pipeline, the outlet in described second sodium carbonate alkali lye pond (12) is connected with secondary Aerobic Pond (13) by pipeline, described secondary Aerobic Pond (13) is connected with medicament pond (14) by pipeline, Calcified pond (141) and flocculation basin (142) is provided with in described medicament pond (14), the import of described Calcified pond (141) is connected with secondary Aerobic Pond (13), the outlet of described Calcified pond (141) is connected with flocculation basin (142), the outlet of described flocculation basin (142) is connected with dephosphorization settling tank (15), the liquid outlet of described dephosphorization settling tank (15) is connected with acidification pool (16), the liquid outlet of described acidification pool (16) is connected with the double oxygen pool (17),
Described wet storage holder (62) comprises tank body (621), the floating cover (622) of gas tank is provided with in described tank body (621), the sidewall of described tank body (621) is provided with vertical guide, guide rail on the corresponding tank body (621) in bottom of the floating cover (622) of described gas tank is provided with lower sheave (623), described lower sheave (623) is slidably connected in the vertical guide of tank body (621), the sidewall of the floating cover (622) of described gas tank is provided with vertical guide, the upper end tank mouth of described tank body (621) is circumferentially provided with top sheave (624), described top sheave (624) is slidably connected in the vertical guide of the floating cover (622) of gas tank, the upper position near tank mouth of described tank body (621) is provided with annular seal-water tank (625), described annular seal-water tank (625) extends to the top of tank body (621), the bottom of described tank body (621) is provided with inlet mouth (626), the top of the floating cover (622) of described gas tank is provided with manhole (627), venting hole (628) and relief hole (629).
Adopt such scheme, grid are mainly used in the preliminary removal to bulk foreign material in water after sewage network accesses sewage work; The agitated pool that catchments stirs residuals in sewage and pumps into solid-liquid separating machine.The effect of solid-liquid separating machine is separated by suspended matter larger for particle diameter in sewage, and isolated material can be used for organic fertilizer production.Just the heavy hydrolysis acidification pool Main Function that regulates is runoff investigation and the tiny foreign material of preliminary precipitation, ensures that follow-up water treatment building normally runs. also play the function of larger molecular organics in acidication waste water.IC reactor decomposing organic matter, and a large amount of COD, BOD removed in waste water produces the reaction unit of biogas.After IC reactor, liquid enters one-level anoxic pond and one-level Aerobic Pond, utilize the pond of microbiological deterioration organism process, in anoxic pond, denitrifying bacterium utilizes the organism carbon source in waste water, be that nitrogen is discharged in air by bringing a large amount of nitrate-nitrogen reduction in backflow mixed liquor into, therefore, BOD declines, and nitrate declines.
Acidic substance during first sodium carbonate alkali lye pond is used for and in water, make water be weakly alkaline, are conducive to microbial growth.Improve the efficiency of aerobic reaction.
In one-level Aerobic Pond, organism is degraded by microbial biochemical and continues to decline, and organonitrogen is by ammonification and then nitrated, be ammonia nitrogen concentration decline, but along with digestive process be nitrate increase, P is along with the excessive extraction of polyP bacteria, enter in bacterium, P content in sewage is declined.
One-level Aerobic Pond water out enters medium sediment pool, again precipitates, the excess sludge in removing Aerobic Pond, makes pond, front end remain active.
Intermediate sedimentation pond secondary anoxic pond and secondary Aerobic Pond react further, and more the process of plus depth remaining COD, BOD, makes water quality be cleaned further, process in rear end to polyP bacteria simultaneously.Second sodium carbonate alkali lye pond is also to regulate pH, makes applicable microbial growth, improves the efficiency of aerobic treatment.
From secondary Aerobic Pond out after, enter Calcified pond and flocculation basin and dephosphorization settling tank, the unnecessary polyP bacteria produced processed, the polyP bacteria of excessive suction phosphorus is removed from waste water, thus reaches the function of dephosphorization; Simultaneously to remaining excess sludge of generation precipitation.And by adding acid for adjusting pH, improve effluent quality.
Finally enter the double oxygen pool.Effect utilizes the microorganism in pool and algae to carry out a biological disposal upon to sewage and organic waste water, carries out waste water evolution, purify water further by " bath bacterium cogeneration system " in pool.This water quality is just recoverable after sterilization.
Biogas is stored, good sealing effect, two cover Guide rollers systems, the possibility that reduction accident occurs, safety and reliability by wet storage holder.This kind of tank body does not arrange civil engineering part, and mobility is strong.
In such scheme: the side of described tank body (621) is provided with staircase (6210).Easy access.
In such scheme: described one-level Aerobic Pond (9) is provided with refluxing opening, and this refluxing opening is connected with one-level anoxic pond (7) by pipeline.
In such scheme: described secondary Aerobic Pond (13) is provided with refluxing opening, and this refluxing opening is connected with secondary anoxic pond (11) by pipeline.
In such scheme: the described double oxygen pool (17) is connected with sterilization pool (18).
In such scheme: the middle part in described one-level Aerobic Pond (9) and secondary Aerobic Pond (13) is equipped with filler (19), and the base plate of described one-level Aerobic Pond (9) and secondary Aerobic Pond (13) is equipped with aeration tube (20).
In such scheme: the base plate of described intermediate sedimentation pond (10) is respectively equipped with sludge collecting board (21), described sludge collecting board (21) indention distributes, and the bottom in the middle of every two sludge collecting boards (21) is provided with shore pipe (22).
Beneficial effect: the utility model designs this process system according to the feature of feces of farm waste water, good sewage processing effect, final energy qualified discharge, behind SPC-D alkali lye pond, anoxic pond and Aerobic Pond is entered from IC reactor waste water out, be conducive to microbial growth, improve the efficiency of anoxic and aerobic treatment, while sewage disposal, produce biogas.
Accompanying drawing illustrates:
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of Aerobic Pond;
Fig. 3 is the structural representation in intermediate sedimentation pond;
Fig. 4 is the structural representation of medicament pond and dephosphorization settling tank;
Fig. 5 is the structural representation of wet storage holder;
Fig. 6 is the vertical view of tank body.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is further described:
Embodiment 1
As shown in figures 1 to 6: Novel cultivation Sewage treatment systems of the present utility model is by grating tank 1, catchment agitated pool 2, solid-liquid separating machine 3, just heavy adjustment hydrolysis acidification pool 4, IC reactor 5, sludge gas collecting device, one-level anoxic pond 7, first sodium carbonate alkali lye pond 8, one-level Aerobic Pond 9, intermediate sedimentation pond 10, secondary anoxic pond 11, second sodium carbonate alkali lye pond 12, secondary Aerobic Pond 13, medicament pond 14, dephosphorization settling tank 15, acidification pool 16, the double oxygen pool 17, sterilization pool 18, filler 19, aeration tube 20, the parts compositions such as sludge collecting board 21 and shore pipe 22.
The water outlet of grating tank 1 is connected with the agitated pool 2 that catchments, catchment in agitated pool 2 and be provided with stirrer 2a, the water outlet of agitated pool 2 of catchmenting is extracted into solid-liquid separating machine 3 by pump, the liquid exit of solid-liquid separating machine 3 is connected to just heavy adjustment hydrolysis acidification pool 4 by pipeline, just the heavy bottom of hydrolysis acidification pool 4 that regulates is provided with sludge pump 4a, just the heavy liquid exit of hydrolysis acidification pool 4 that regulates is connected with the import of IC reactor 5, the upper outlet body of IC reactor 5 is provided with sludge gas collecting device, and sludge gas collecting device comprises methane purifying device 61 and wet storage holder 62.The venting port of wet storage holder 62 is connected with user.Wet storage holder 62 comprises tank body 621, the bottom of tank body 621 is provided with pedestal, be provided with gas tank in tank body 621 and float cover 622, the sidewall of tank body 621 is provided with vertical guide, the guide rail that gas tank floats on the corresponding tank body 621 in bottom of cover 622 is provided with lower sheave 623, lower sheave 623 is slidably connected in the vertical guide of tank body 621, the sidewall that gas tank floats cover 622 is provided with vertical guide, the upper end tank mouth of tank body 621 is circumferentially provided with top sheave 624, the tank mouth of tank body 621 is provided with in-flanges, top sheave 624 is arranged on in-flanges by pulley bracket, top sheave 624 is slidably connected at gas tank and floats in the vertical guide of cover 622, position near tank mouth on tank body 621 is provided with annular seal-water tank 625, annular seal-water tank 625 reaches the top of tank body 621, top sheave 624 is positioned at annular seal-water tank 625, the bottom of tank body 621 is provided with inlet mouth 626, the top that gas tank floats cover 622 is provided with manhole 627, venting hole 628 and relief hole 629.The side of tank body 621 is provided with staircase 6210.Easy access.This wet storage holder does not have civil engineering part, mobility is strong, biogas enters in tank body 621 from inlet mouth 626, pressure increase, gas tank floats cover 622 and moves up, sliding system comprises vertical guide and circumference on lower sheave 623 and tank body 621 and is arranged on top sheave 624 on tank body 621 tank mouth and gas tank and floats vertical guide on cover 622, and such gas tank floats cover 622 and slides up and down more freely, slides more reliable.
IC reactor 5 is high efficiency anaerobic reactor again.The liquid exit of IC reactor 5 is connected with one-level anoxic pond 7 by pipeline, the outlet of one-level anoxic pond 7 is connected with the first sodium carbonate alkali lye pond 8, by the pH value of the first sodium carbonate alkali lye pond 8 regulates liquid, be conducive to microbial growth, the outlet in the first sodium carbonate alkali lye pond 8 is connected with one-level Aerobic Pond 9, one-level Aerobic Pond 9 is provided with refluxing opening, and this refluxing opening is connected with one-level anoxic pond 7 by pipeline.The outlet of one-level Aerobic Pond 9 is connected with intermediate sedimentation pond 10 by pipeline, the water outlet in intermediate sedimentation pond 10 is connected with secondary anoxic pond 11 by pipeline, secondary anoxic pond 11 is connected with the second sodium carbonate alkali lye pond 12, the outlet in the second sodium carbonate alkali lye pond 12 is connected with secondary Aerobic Pond 13 by pipeline, secondary Aerobic Pond 13 is provided with refluxing opening, and this refluxing opening is connected with secondary anoxic pond 11 by pipeline.Secondary Aerobic Pond 13 is connected with medicament pond 14 by pipeline, Calcified pond 141 and flocculation basin 142 is provided with in medicament pond 14, the import of Calcified pond 141 is connected with secondary Aerobic Pond 13, the outlet of Calcified pond 141 is connected with flocculation basin 142, stirrer is provided with in flocculation basin 142, the outlet of flocculation basin 142 is connected with dephosphorization settling tank 15, and the liquid outlet of dephosphorization settling tank 15 is connected with acidification pool 16, and the liquid outlet of acidification pool 16 is connected with the double oxygen pool 17.The double oxygen pool 17 is connected with sterilization pool 18.
Middle part in one-level Aerobic Pond 9 and secondary Aerobic Pond 13 is equipped with filler 19, the base plate of one-level Aerobic Pond 9 and secondary Aerobic Pond 13 is equipped with aeration tube 20.Described aeration tube 20 is connected with gas blower 23.The base plate in intermediate sedimentation pond 10 is respectively equipped with sludge collecting board 21, sludge collecting board 21 indention distributes, and the bottom in the middle of every two sludge collecting boards 21 is provided with shore pipe 22.
Described dephosphorization settling tank 15 comprises pond body 151, water-in 152 is provided with on the top of the right side wall of pond body 151, the top of left side wall is provided with water outlet 153, the middle part of described pond body 151 is provided with vertical baffle 154, distance is had between this vertical baffle 154 and base plate of pond body 151, packing layer 155 is provided with between the lower end of described vertical baffle 154 and the left side wall of pond body 151, baffle plate 156 is provided with before described water-in 152, on the top cover of described baffle plate 156 device pond body 151, the lower end of described baffle plate 156 extends to below water-in 152, the base plate of described pond body 151 is also provided with sludge collecting board 21, described sludge collecting board 21 indention distribution, the bottom of the centre of described sludge collecting board 21 is provided with shore pipe 22, described dephosphorization settling tank 15, just the heavy mud of the bottom in hydrolysis acidification pool 4 and intermediate sedimentation pond 10 that regulates is extracted into sludge drying pond by sludge pump, mummifying pool effect is solid-liquid separation, mud to enter after mummifying pool precipitate and separate under gravity, clear liquid enters perforated tube from bottom, dry-matter is by manually removing.
More than describe preferred embodiment of the present utility model in detail.Should be appreciated that those of ordinary skill in the art just can make many modifications and variations according to design of the present utility model without the need to creative work.Therefore, all technician in the art according to design of the present utility model on the basis of existing technology by the available technical scheme of logical analysis, reasoning, or a limited experiment, all should by the determined protection domain of claims.
Claims (7)
1. a Novel cultivation Sewage treatment systems, comprise grating tank (1), it is characterized in that: the water outlet of described grating tank (1) is connected with the agitated pool that catchments (2), stirrer (2a) is provided with in the described agitated pool that catchments (2), the water outlet of the described agitated pool that catchments (2) is extracted into solid-liquid separating machine (3) by pump, the liquid exit of described solid-liquid separating machine (3) is connected to just heavy adjustment hydrolysis acidification pool (4) by pipeline, the described just heavy bottom of hydrolysis acidification pool (4) that regulates is provided with sludge pump, the described just heavy liquid exit of hydrolysis acidification pool (4) that regulates is connected with the import of IC reactor (5), air outlet on the upper outlet body of described IC reactor (5) is connected with methane purifying device (61) by pipeline, the outlet of described methane purifying device (61) is connected with wet storage holder (62) by pipeline, the liquid exit of described IC reactor (5) is connected with one-level anoxic pond (7) by pipeline, the outlet of described one-level anoxic pond (7) is connected with the first sodium carbonate alkali lye pond (8), the outlet in described first sodium carbonate alkali lye pond (8) is connected with one-level Aerobic Pond (9), the outlet of described one-level Aerobic Pond (9) is connected with intermediate sedimentation pond (10) by pipeline, the water outlet of described intermediate sedimentation pond (10) is connected with secondary anoxic pond (11) by pipeline, described secondary anoxic pond (11) is connected with the second sodium carbonate alkali lye pond (12) by pipeline, the outlet in described second sodium carbonate alkali lye pond (12) is connected with secondary Aerobic Pond (13) by pipeline, described secondary Aerobic Pond (13) is connected with medicament pond (14) by pipeline, Calcified pond (141) and flocculation basin (142) is provided with in described medicament pond (14), the import of described Calcified pond (141) is connected with secondary Aerobic Pond (13), the outlet of described Calcified pond (141) is connected with flocculation basin (142), the outlet of described flocculation basin (142) is connected with dephosphorization settling tank (15), the liquid outlet of described dephosphorization settling tank (15) is connected with acidification pool (16), the liquid outlet of described acidification pool (16) is connected with the double oxygen pool (17),
Described wet storage holder (62) comprises tank body (621), the floating cover (622) of gas tank is provided with in described tank body (621), the sidewall of described tank body (621) is provided with vertical guide, guide rail on the corresponding tank body (621) in bottom of the floating cover (622) of described gas tank is provided with lower sheave (623), described lower sheave (623) is slidably connected in the vertical guide of tank body (621), the sidewall of the floating cover (622) of described gas tank is provided with vertical guide, the upper end tank mouth of described tank body (621) is circumferentially provided with top sheave (624), described top sheave (624) is slidably connected in the vertical guide of the floating cover (622) of gas tank, the upper position near tank mouth of described tank body (621) is provided with annular seal-water tank (625), described annular seal-water tank (625) extends to the top of tank body (621), the bottom of described tank body (621) is provided with inlet mouth (626), the top of the floating cover (622) of described gas tank is provided with manhole (627), venting hole (628) and relief hole (629).
2. Novel cultivation Sewage treatment systems according to claim 1, is characterized in that: the side of described tank body (621) is provided with staircase (6210).
3. Novel cultivation Sewage treatment systems according to claim 1, is characterized in that: described one-level Aerobic Pond (9) is provided with refluxing opening, and this refluxing opening is connected with one-level anoxic pond (7) by pipeline.
4. Novel cultivation Sewage treatment systems according to claim 3, is characterized in that: described secondary Aerobic Pond (13) is provided with refluxing opening, and this refluxing opening is connected with secondary anoxic pond (11) by pipeline.
5. Novel cultivation Sewage treatment systems according to claim 1, is characterized in that: the described double oxygen pool (17) is connected with sterilization pool (18).
6. Novel cultivation Sewage treatment systems according to claim 1, it is characterized in that: the middle part in described one-level Aerobic Pond (9) and secondary Aerobic Pond (13) is equipped with filler (19), and the base plate of described one-level Aerobic Pond (9) and secondary Aerobic Pond (13) is equipped with aeration tube (20).
7. Novel cultivation Sewage treatment systems according to claim 1, it is characterized in that: the base plate of described intermediate sedimentation pond (10) is respectively equipped with sludge collecting board (21), described sludge collecting board (21) indention distributes, and the bottom in the middle of every two sludge collecting boards (21) is provided with shore pipe (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420736447.0U CN204342604U (en) | 2014-11-28 | 2014-11-28 | Novel cultivation Sewage treatment systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420736447.0U CN204342604U (en) | 2014-11-28 | 2014-11-28 | Novel cultivation Sewage treatment systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204342604U true CN204342604U (en) | 2015-05-20 |
Family
ID=53225889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420736447.0U Withdrawn - After Issue CN204342604U (en) | 2014-11-28 | 2014-11-28 | Novel cultivation Sewage treatment systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204342604U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104445817A (en) * | 2014-11-28 | 2015-03-25 | 重庆甘泰环保设备有限公司 | Novel farming sewage treatment system |
-
2014
- 2014-11-28 CN CN201420736447.0U patent/CN204342604U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104445817A (en) * | 2014-11-28 | 2015-03-25 | 重庆甘泰环保设备有限公司 | Novel farming sewage treatment system |
| CN104445817B (en) * | 2014-11-28 | 2016-03-30 | 重庆力华环保工程有限公司 | A kind of aquaculture wastewater treatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104402175B (en) | A kind of pig farm breeding wastewater biochemical treatment system | |
| CN100406399C (en) | Method and system for harnessing consumer waste landfill percolate | |
| CN108483804A (en) | A kind of scale animal and poultry cultivation liquid dung recycling comprehensive processing technique | |
| CN105271610A (en) | Comprehensive processing process of culturing farm cow dung waste water | |
| CN103319056B (en) | Hospital sewage treatment system | |
| CN206486407U (en) | A kind of livestock breeding wastewater processing system | |
| CN105859033A (en) | Domestic sewage treatment process | |
| CN104310714A (en) | System for processing breeding and slaughtering sewage and technology for system | |
| CN106946403A (en) | UASB two-stage A/O coagulating treatments pig farm biogas slurry technique | |
| CN207713595U (en) | Sewage treatment system for farm | |
| CN204342610U (en) | Pig farm breeding wastewater biochemical treatment system | |
| CN204342601U (en) | Aquaculture wastewater treatment system | |
| CN205313324U (en) | AMBR integration sewage treatment device | |
| CN210620525U (en) | Water-fertilizer co-production device for breeding manure | |
| CN205347142U (en) | Aquaculture wastewater treatment system | |
| CN219194742U (en) | Low-energy-consumption sewage treatment system | |
| CN204342604U (en) | Novel cultivation Sewage treatment systems | |
| CN104445817B (en) | A kind of aquaculture wastewater treatment system | |
| CN205856280U (en) | A kind of rural sewage treatment system | |
| CN206437996U (en) | A kind of cultivating wastewater purification device | |
| CN106064870A (en) | A kind of cultivating wastewater purification device | |
| CN104445616A (en) | Vertical continuous flow phosphorus removing device and method | |
| CN107540160A (en) | Cultivation wastewater purification handling process and its device | |
| CN210313923U (en) | Energy-efficient breed effluent disposal system | |
| CN208995353U (en) | A kind of sewage disposal system with automatic control |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150520 Effective date of abandoning: 20160330 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |