CN206843188U - The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique - Google Patents
The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique Download PDFInfo
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- CN206843188U CN206843188U CN201720496901.3U CN201720496901U CN206843188U CN 206843188 U CN206843188 U CN 206843188U CN 201720496901 U CN201720496901 U CN 201720496901U CN 206843188 U CN206843188 U CN 206843188U
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- container body
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- 238000000034 method Methods 0.000 title claims abstract description 45
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 244000005700 microbiome Species 0.000 claims abstract description 17
- 238000005273 aeration Methods 0.000 claims abstract description 16
- 239000000945 filler Substances 0.000 claims abstract description 9
- 238000002513 implantation Methods 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims abstract description 7
- 239000011229 interlayer Substances 0.000 claims abstract description 6
- 239000010410 layer Substances 0.000 claims abstract description 5
- 239000000725 suspension Substances 0.000 claims abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 27
- 241000196324 Embryophyta Species 0.000 claims description 24
- 239000003610 charcoal Substances 0.000 claims description 13
- 229910052742 iron Inorganic materials 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 11
- 239000012876 carrier material Substances 0.000 claims description 7
- 241000309551 Arthraxon hispidus Species 0.000 claims description 6
- 240000008436 Ipomoea aquatica Species 0.000 claims description 6
- 235000019004 Ipomoea aquatica Nutrition 0.000 claims description 6
- 230000003044 adaptive effect Effects 0.000 claims description 6
- 230000000855 fungicidal effect Effects 0.000 claims description 4
- 239000000417 fungicide Substances 0.000 claims description 4
- 238000006213 oxygenation reaction Methods 0.000 claims description 4
- 235000017060 Arachis glabrata Nutrition 0.000 claims description 3
- 244000105624 Arachis hypogaea Species 0.000 claims description 3
- 235000010777 Arachis hypogaea Nutrition 0.000 claims description 3
- 235000018262 Arachis monticola Nutrition 0.000 claims description 3
- 244000025254 Cannabis sativa Species 0.000 claims description 3
- 244000099162 Cyperus alternifolius Species 0.000 claims description 3
- 240000003826 Eichhornia crassipes Species 0.000 claims description 3
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- 235000000365 Oenanthe javanica Nutrition 0.000 claims description 3
- 235000020232 peanut Nutrition 0.000 claims description 3
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 238000004065 wastewater treatment Methods 0.000 claims description 3
- 230000000813 microbial effect Effects 0.000 claims description 2
- 229910017112 Fe—C Inorganic materials 0.000 claims 1
- 238000000746 purification Methods 0.000 abstract description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- 241000894006 Bacteria Species 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000010865 sewage Substances 0.000 description 8
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 239000011574 phosphorus Substances 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000012851 eutrophication Methods 0.000 description 3
- 238000006396 nitration reaction Methods 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
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- 239000004912 1,5-cyclooctadiene Substances 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 206010059410 Faecaluria Diseases 0.000 description 1
- 244000186654 Fockea angustifolia Species 0.000 description 1
- 235000015210 Fockea angustifolia Nutrition 0.000 description 1
- 241000186660 Lactobacillus Species 0.000 description 1
- 241000108664 Nitrobacteria Species 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
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- 238000006065 biodegradation reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
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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
- Biological Treatment Of Waste Water (AREA)
Abstract
The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique, including：Tabular floating body, the tabular floating body includes upper kickboard, lower kickboard and the interlayer between upper kickboard, lower kickboard, kickboard offers multiple implantation holes on this, kind is implanted with water plant in each implantation hole, middle part upper end of kickboard is provided with air pump on this, the appendix that connection one extends downwardly below the gas outlet of the air pump, the lower end of the appendix connects more aeration tubes；Multiple containers body, each container body hangs on the lower end of lower kickboard by a suspension ring, there are multiple mesh in the side wall of each container body, if each container body is provided with dried layer every sieve plate in the height direction, the filler for purifying water body is filled with each container body, the bottom of each container body is hung with balancing weight.Tank body, multiple sieve apertures are offered in the side wall and bottom wall of the tank body, complex microorganism material is filled with the tank body.The utility model is used for reach the saving energy, efficiently the purpose for the treatment of and purification water quality.
Description
Technical field
The technical field that restoration of the ecosystem processing is carried out to piggery wastewater is the utility model is related to, more particularly at piggery wastewater
The terminal oxidized pool purifier of science and engineering skill.
Background technology
With the development of Urbanization in China, because Large-scale pig farm and livestock and poultry breeding industry are quickly grown, Er Qiegui
Mould constantly expands.Scale pig farm is the economic benefit that covets for a long time, and environmental consciousness is weak, to fecal sewage treatment
Method falls behind, and causes the organic sewage of substantial amounts of high concentration to be discharged into rivers and lakes, causes water quality constantly to deteriorate, wherein in sewage
Nitrogen, the phosphorus of high concentration are the main reason for causing body eutrophication.Most of pig farm plants do not consider excrement building an initial stage
Just handle, a large amount of fecalurias of piggery wastewater discharge and a large amount of waste water of plant, mostly without properly recycling and processing, place
I.e. direct discharge is put, serious pollution is caused to environment.Surrounding city piggery wastewater has become or turned into and Industry Waste
Water and the quite even more big pollution sources of sanitary sewage.The processing work of piggery wastewater has been carried out on China pig farm at present, its institute
The technology path of use mainly has anaerobic treatment process (hydraulic type biomass pool)；Efficient anaerobic handles (UASB)+Aerobic Process for Treatment
(SBR)；Aerobic treatment process (aeration oxidation pond+biological stabilization pond) etc. is several.In spite of these processing methods, piggery wastewater
Handling rate is still very low, and the sewage of some pig farms discharge still contains compared with pollutants such as high organic, nitrogen and phosphorus, causes local life
State environment and the serious pollution in farmland.
Aquatic plant ecological floating bed purifies water applied to oxidation pond in recent years, is also used for the end of livestock and poultry breeding industry water body
Processing.Existing biologic float bed technology relies primarily on nutrients and the organic matters such as plant absorption N, the P planted in floating bed, due to by
Season and the limitation of floating bed plant, it only utilizes surface water for fluitante, and plant is limited to water body purification effect,
In the extremely low eutrophication of dissolved oxygen even in water body undergrowth, maintenance is difficult, cost is higher, and its clean-up effect is difficult
Further improve.For high nitrogen, phosphorus and organic matter, in water body at the relatively low pig farm aquaculture water body oxidation pond of dissolved oxygen content
Reason, lacks effective purification techniques.
Utility model content
In view of the shortcomings of the prior art, it is net to aim to provide a kind of terminal oxidized pool of Process for Treatment of Swine Wastewater technique for the utility model
Makeup is put, to reach the saving energy, the efficiently purpose for the treatment of and purification water quality.
To achieve the above object, the utility model adopts the following technical scheme that：
The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique, including：
Tabular floating body, the tabular floating body include upper kickboard, lower kickboard and the interlayer between upper kickboard, lower kickboard,
Kickboard offers multiple implantation holes on this, and kind is implanted with water plant in each implantation hole, root of the interlayer for plant of supplying water
System's growth, middle part upper end of kickboard is provided with air pump on this, the appendix that connection one extends downwardly below the gas outlet of the air pump,
The lower end of the appendix connects more aeration tubes, and the aeration tube is used to be filled with air to water body；
Multiple containers body, each container body hang on the lower end of lower kickboard, the side wall of each container body by a suspension ring
Upper have multiple mesh, if each container body in sieve plate, each container body in the height direction provided with dried layer every being filled with use
In the filler of purifying water body, the bottom of each container body is hung with balancing weight.
The tank body of appendix upper end peripheral region is fixed on, offers multiple sieve apertures in the side wall and bottom wall of the tank body, the tank
It is filled with complex microorganism material in vivo.
Preferably, the terminal oxidized pool purifier of the Process for Treatment of Swine Wastewater technique also includes a solar powered dress
Put, be installed on the top of air pump, including support frame, photovoltaic board component, battery, support frame as described above is used to carry to photovoltaic board component
For brace foundation, the battery is electrically connected at photovoltaic board component and is fixed on support frame, is provided with support frame as described above
Universal spherical joint head, the universal spherical joint head are used for the light angle for adjusting photovoltaic board component, and the battery is used
Powered in air pump.
Preferably, the multiple container body is circumferentially suspended to the lower end of lower kickboard in array.
Preferably, the filler is compound porous iron charcoal (Fe-C) biological carrier materials of denitrogenation.
Preferably, the aeration tube is porous nano oxygenation aeration pipe.
Preferably, the complex microorganism material is complex micro organism fungicide.
Preferably, the water plant can be water spinach, water spinach, oenanthe stolonifera, cyperus alternifolius, ruthless tail grass, Eichhornia crassipes or water
Peanut, plantation density of the water plant on tabular floating body are 15~25 plants/m2。
Preferably, the terminal oxidized pool purifier of the Process for Treatment of Swine Wastewater technique also includes a civil power adaptive device, should
Civil power adaptive device is used to connect outside mains supply.
Compared to prior art, beneficial effect possessed by the utility model is：
1. producing electric energy using solar energy drives air pump work, it is not necessary to external power supply electric energy is consumed, can be with effectively save
The energy, it is applied widely；
2. under conditions of the aeration aerating of air pump, oxygen in water concentration is added, promotion is played to biodegradation and is made
With effectively reducing pollutional load, efficiently go organic matter and other pollutants such as COD, nitrogen, phosphorus, purifying water body water quality in water removal；
3. the content of microorganisms in surrounding water and on filler is effectively increased by microorganism tank, efficiently in degradation water
N, the organic pollution such as P, water body purification effect is further improved.
4. compound porous iron charcoal (Fe-C) biological carrier materials of denitrogenation, ammonia oxidation bacteria and nitrification are thin under iron charcoal aerobic condition
Bacterium quickly nitrifies ammonia nitrogen in water, realizes synchronous nitration and denitrification fast deep denitrogenation, is to collect technology of biological membrane, itself chemistry instead
Technology is answered in one advanced nitrogen technology in situ.
5. pair water environment carries out three-dimensional reparation.Kind is implanted with water plant on tabular floating body, underwater setting microorganism tank, and
There is the multiple containers body for being filled with denitrogenation composite holes iron charcoal (Fe-C) bio-carrier, three's formation one is biological floating bed, right
Water body carries out multi-level improvement, comprehensive fast purification water quality, substantially increases pollution control efficiency.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the cross section view at Figure 1A-A places；
Fig. 3 is top view of the present utility model；
Wherein, 1, photovoltaic board component；2nd, support frame；3rd, universal spherical joint head；4th, air pump；5th, water plant；6th, plate
Shape floating body；7th, every sieve plate；8th, appendix；9th, container body；10th, aeration tube；11st, battery；12nd, suspension ring；13rd, balancing weight；14th, it is empty
Flighty and impatient circle；15th, the water surface；16th, tank body.
Embodiment
Below, with reference to accompanying drawing and specific embodiment, the utility model is described further：
As shown in Figure 1-Figure 3, the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique, including：
Tabular floating body 6, the tabular floating body 6 include upper kickboard, lower kickboard and the folder between upper kickboard, lower kickboard
Layer, kickboard offers multiple implantation holes on this, and kind is implanted with water plant 5 in each implantation hole, and the interlayer is used for plant 5 of supplying water
Root growth, middle part upper end of kickboard is provided with air pump 4 on this, below the gas outlet of the air pump 4 connection one extend downwardly
Appendix 8, the lower end of the appendix 8 connect more aeration tubes 10, and the aeration tube 10 is used to be filled with air to water body；
Multiple containers body 9, each container body 9 hang on the lower end of lower kickboard by a suspension ring 12, each container body 9
There are multiple mesh, if each container body 9 fills provided with dried layer every in sieve plate 7, each container body 9 in the height direction in side wall
The filler for purifying water body is filled with, the bottom of each container body 9 is hung with balancing weight 13.
The tank body 16 of appendix upper end peripheral region is fixed on, multiple sieve apertures are offered in the side wall and bottom wall of the tank body 16,
Complex microorganism material is filled with the tank body 16.
As a kind of preferable scheme, the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique also includes one too
Positive energy electric supply installation, the top of air pump 4 is installed on, including support frame 2, photovoltaic board component 1, battery 11, support frame as described above 2 are used
In providing brace foundation to photovoltaic board component 1, the battery 11 is electrically connected at photovoltaic board component 1 and is fixed on support frame 2
On, universal spherical joint head 3 is provided with support frame as described above 2, the universal spherical joint head 3 is used to adjust photovoltaic board component
1 light angle, the battery 11 are used to power to air pump 4.
As a kind of preferable scheme, the multiple container body 9 is circumferentially suspended to the lower end of lower kickboard in array.
As a kind of preferable scheme, the filler is compound porous iron charcoal (Fe-C) biological carrier materials of denitrogenation.It is described
The compound porous iron charcoal Fe-C biological carrier materials of denitrogenation, it is to be apt to refined .2014. according to Zhu《The preparation of denitrogenation compound bio carrier and
It is in low C/N than the application study in sewage water denitrification processing》[D] Beijing：What Beijing Jiaotong University's master thesis was implemented.
Result of study described in the paper shows：The preparation method of the filler be using iron powder, active powdered carbon and catalyst as raw material,
(surface mainly contains the elements such as iron, charcoal, oxygen, adhesive, catalyst, its quality is respectively 51.86%, 36.97%, 6.33%,
3.53%th, adhesive 1.31%) is added, then granulating and forming, then carry out high-temperature roasting under anaerobic, is fired into particle diameter about
For the 5~10mm compound porous iron charcoal Fe-C biological carrier materials of denitrogenation.It would know that by result of the test, the compound porous iron charcoal of denitrogenation
Fe-C bio-carriers in low C/N than sewage water denitrification processing, imitate by the purification for all having more efficient under acid, neutral, alkalescence condition
Fruit.
As a kind of preferable scheme, the aeration tube 10 is porous nano oxygenation aeration pipe.
As a kind of preferable scheme, the complex microorganism material is complex micro organism fungicide.The composite microbial bacteria
The component of agent refers to Publication No. CN104211184B, a kind of entitled " microorganism sewage water for being used to raise value wastewater treatment
The patent of invention of inorganic agent ", is calculated by weight, the complex micro organism fungicide include 10~20 parts nitrobacteria, 15~30 parts
Denitrifying bacteria, 10~50 parts of bacillus, 5~20 parts of biology enzymes, 5~15 parts of lactobacillus, 10~20 parts of yeast floras, 20
~40 parts of photosynthetic bacteria groups, wherein, contain in monoxenic every gram of culture medium and be not less than 2.0 hundred million active bacterias.
As a kind of preferable scheme, the water plant 5 can be water spinach, water spinach, oenanthe stolonifera, cyperus alternifolius, ruthless tail
Grass, Eichhornia crassipes or water peanut, plantation density of the water plant 5 on tabular floating body 6 are 15~25 plants/m2。
As a kind of preferable scheme, the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique also includes a civil power
Adaptive device, the civil power adaptive device are used to connect outside mains supply.
The terminal oxidized pool purifier cleaning principle of Process for Treatment of Swine Wastewater technique described in the utility model：The utility model
Built with tabular floating body 6 biologic float bed, make full use of solar energy to drive the air pump 4 of oxygen processed, oxygenation whole for the biological floating bed enhancing
The dissolved oxygen ability of individual system, provide and fill for the microorganism growth of compound porous iron charcoal (Fe-C) bio-carrier of underwater denitrogenation
The oxygen of foot, and increase the content of Dissolved Oxygen in Water, microorganism tank greatly increases the quantity of microorganism in biologic float bed system,
The efficiently organic pollution such as N, P in degradation water, and then clean-up effect of increasing water quality.Institute's growing plant absorbs and gone on biological floating bed
The nutrients such as nitrogen, phosphorus in water removal, suppression algal grown can be played, eliminate body eutrophication, improve the work of water transparency
With.
In addition, compound porous iron charcoal (Fe-C) biological carrier materials of denitrogenation ammonia oxidation bacteria and nitrification under iron charcoal aerobic condition
Bacterium quickly nitrifies ammonia nitrogen in water, while denitrifying bacterium utilizes nascent state caused by Fe-C itself chemical reactions inside biomembrane
[H] and [Fe2+] for anti-nitration reaction electronics is provided, realize synchronous nitration and denitrification fast deep denitrogenation；Fe-C in course of reaction
Itself chemical reaction provides electronics for denitrification, greatly reduces the carbon source consumption of denitrification process.It is therefore not necessary to external carbon
Source, polluted-water fast denitrogenation can be achieved under the conditions of aerobic, low C/N ratios, be collection technology of biological membrane, itself chemical reaction technology
In integral advanced nitrogen technology.
It will be apparent to those skilled in the art that technical scheme that can be as described above and design, make other various
Corresponding change and deformation, and all these changes and deformation should all belong to the protection of the utility model claims
Within the scope of.
Claims (8)
1. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique, it is characterised in that including：
Tabular floating body, the tabular floating body include upper kickboard, lower kickboard and the interlayer between upper kickboard, lower kickboard, on this
Kickboard offers multiple implantation holes, and kind is implanted with water plant in each implantation hole, root system life of the interlayer for plant of supplying water
Long, middle part upper end of kickboard is provided with air pump on this, the appendix that connection one extends downwardly below the gas outlet of the air pump, described
The lower end of appendix connects more aeration tubes, and the aeration tube is used to be filled with air to water body；
Multiple containers body, each container body are hung on the lower end of lower kickboard by a suspension ring, had in the side wall of each container body
There are multiple mesh, if each container body is provided with dried layer every being filled with sieve plate, each container body for net in the height direction
Change the filler of water body, the bottom of each container body is hung with balancing weight；
The tank body of appendix upper end peripheral region is fixed on, multiple sieve apertures are offered in the side wall and bottom wall of the tank body, in the tank body
It is filled with complex microorganism material.
2. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：The pig farm
The terminal oxidized pool purifier of waste water treatment process also includes a solar power supply apparatus, is installed on the top of air pump, including
Support frame, photovoltaic board component, battery, support frame as described above are used to provide brace foundation, the storage battery to photovoltaic board component
Property is connected to photovoltaic board component and is fixed on support frame, universal spherical joint head is provided with support frame as described above, this is universal
Ball pivot head is used for the light angle for adjusting photovoltaic board component, and the battery is used to power to air pump.
3. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：It is the multiple
Container body is circumferentially suspended to the lower end of lower kickboard in array.
4. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：The filler
For the compound porous iron charcoal Fe-C biological carrier materials of denitrogenation.
5. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：The aeration
Manage as porous nano oxygenation aeration pipe.
6. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：It is described compound
Microbial material is complex micro organism fungicide.
7. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：It is described aquatic
Plant can be water spinach, water spinach, oenanthe stolonifera, cyperus alternifolius, ruthless tail grass, Eichhornia crassipes or water peanut, and the water plant is in tabular
Plantation density on floating body is 15~25 plants/m2。
8. the terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique as claimed in claim 1, it is characterised in that：The pig farm
The terminal oxidized pool purifier of waste water treatment process also includes a civil power adaptive device, and the civil power adaptive device is used to connect outside
Mains supply.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720496901.3U CN206843188U (en) | 2017-04-28 | 2017-04-28 | The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720496901.3U CN206843188U (en) | 2017-04-28 | 2017-04-28 | The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206843188U true CN206843188U (en) | 2018-01-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720496901.3U Expired - Fee Related CN206843188U (en) | 2017-04-28 | 2017-04-28 | The terminal oxidized pool purifier of Process for Treatment of Swine Wastewater technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206843188U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775870A (en) * | 2019-04-04 | 2019-05-21 | 湖北理工学院 | An automatic cleaning device that floats on the water surface |
| CN110282757A (en) * | 2019-07-24 | 2019-09-27 | 广东新大禹环境科技股份有限公司 | A kind of black and odorous water pollution amelioration system |
-
2017
- 2017-04-28 CN CN201720496901.3U patent/CN206843188U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775870A (en) * | 2019-04-04 | 2019-05-21 | 湖北理工学院 | An automatic cleaning device that floats on the water surface |
| CN110282757A (en) * | 2019-07-24 | 2019-09-27 | 广东新大禹环境科技股份有限公司 | A kind of black and odorous water pollution amelioration system |
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