CN205061690U - Anaerobism - good oxygen integrative sewage treatment device - Google Patents
Anaerobism - good oxygen integrative sewage treatment device Download PDFInfo
- Publication number
- CN205061690U CN205061690U CN201520636179.XU CN201520636179U CN205061690U CN 205061690 U CN205061690 U CN 205061690U CN 201520636179 U CN201520636179 U CN 201520636179U CN 205061690 U CN205061690 U CN 205061690U
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- Prior art keywords
- pond
- aerobic
- anaerobic
- filter cloth
- good oxygen
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- Expired - Fee Related
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- 239000010865 sewage Substances 0.000 title abstract description 12
- 229910052760 oxygen Inorganic materials 0.000 title abstract description 11
- 239000001301 oxygen Substances 0.000 title abstract description 11
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 title abstract description 11
- 239000004744 fabric Substances 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 238000005273 aeration Methods 0.000 claims abstract description 18
- 241000143392 Oar Species 0.000 claims abstract description 14
- 239000002699 waste material Substances 0.000 claims description 12
- 239000010802 sludge Substances 0.000 claims description 7
- 229920004933 Terylene® Polymers 0.000 claims description 6
- 230000001808 coupling Effects 0.000 claims description 6
- 238000010168 coupling process Methods 0.000 claims description 6
- 238000005859 coupling reaction Methods 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 6
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 6
- 239000004677 Nylon Substances 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229920001778 nylon Polymers 0.000 claims description 3
- -1 polypropylene Polymers 0.000 claims description 3
- 229920001155 polypropylene Polymers 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 229920002554 vinyl polymer Polymers 0.000 claims description 3
- 238000003756 stirring Methods 0.000 abstract description 4
- 239000012528 membrane Substances 0.000 abstract description 3
- 239000005416 organic matter Substances 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000084 colloidal system Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000002906 microbiologic Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000002957 persistent organic pollutant Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 3
- 230000036740 Metabolism Effects 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 230000035786 metabolism Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000005039 chemical industry Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000003247 decreasing Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 230000000813 microbial Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Abstract
The utility model discloses an anaerobism - good oxygen integrative sewage treatment device, including the sewage treatment pond, vertically in the sewage treatment pond set up 4 industrial filter cloth membranes, separate in proper order for first good oxygen pond, first anaerobism pond, the good oxygen pond of second, second anaerobism pond and clear solution storage pool, 2 blowdown mud mouth is all established to individual good oxygen pond and 2 anaerobism pond lower parts, first good oxygen pond upper portion is equipped with the inlet, clear solution storage pool lower part is equipped with the liquid outlet, the good oxygen bottom of the pool portion of first good oxygen pond and second sets up the aeration pipe that has a plurality of aeration holes, the aeration pipe links to each other with the outside air compressor in good oxygen pond, set up agitating unit in first anaerobism pond and the second anaerobism pond, agitating unit includes that the pivot that links to each other with the motor sets up the stirring brush in the both sides of pivot with the symmetry, the stirring brush comprises with the V type brush hair that is fixed in fixed oar both sides the fixed oar of vertical setting, fixed oar is connected through a plurality of connecting axles and pivot, the the device organic matter is got rid of efficiently, saves area, reduces investment cost, and the management is convenient.
Description
Technical field
The utility model belongs to field of Environment Protection, particularly relates to a kind of anaerobic-aerobic integrated waste disposal plant.
Background technology
Organic chemical industry, food-processing, textile printing and dyeing, papermaking, leather, the industry such as medicine, and the organic sewage produced in the industry production such as livestock and poultry cultivation, enter rivers and will cause severe contamination, and then cause water resources to lack and quality of water environment deterioration, Activated Sludge Process in domestic and international improvement treatment of Organic Wastewater, almost all based on the " anaerobism of biology, anoxic, aerobic " growth metabolism is theoretical and realize, namely the organism in sewage, nitrogen, the pollutents such as phosphorus, in biological tank under varying environment, by being removed under microbial growth metabolism, realize the object of purifying water body.
In existing technique there is following problem in great majority: 1) floor space is large, and initial cost is high; 2) sludge liquid backflow, adds power consumption and working cost.
Utility model content
The utility model provides a kind of anaerobic-aerobic integrated waste disposal plant, and organic matter removal efficiency is high, saves floor space, reduces cost of investment, convenient management.
In order to solve the problem, the technical solution adopted in the utility model is such, a kind of anaerobic-aerobic integrated waste disposal plant, comprise treatment tank, 4 pieces of industrial filter cloth films are vertically set in treatment tank, treatment tank is separated into 5 parts, respectively be the first Aerobic Pond, first anaerobic pond, second Aerobic Pond, second anaerobic pond and clear liquid storage pool, sludge discharging port is all established in 2 described Aerobic Ponds and 2 anaerobic pond bottoms, first Aerobic Pond top is provided with fluid inlet, clear liquid storage pool bottom is provided with liquid outlet, the aeration tube of multiple solarization air cap is provided with bottom first Aerobic Pond and the second Aerobic Pond, described aeration tube stretches out outside Aerobic Pond along Aerobic Pond sidewall and is connected with the air compressor being arranged on Aerobic Pond outside, in first anaerobic pond and the second anaerobic pond, a grade whipping appts is set, described whipping appts comprises the Mixing Brush of the rotating shaft be connected with motor and the both sides being symmetricly set on rotating shaft, Mixing Brush is made up of the fixing oar vertically arranged and the V-type bristle being fixed on fixing oar both sides, fixing oar is connected with rotating shaft by multiple coupling shaft.
In order to promote the contact of mud and microorganism further, take away under the effect of filter pressure, be trapped within industrial filter cloth film surface colloid and suspended particle, the V-type of described V-type bristle is opening up, and V-type bristle is preferably made by steel wire, copper wire or nylon material.
In order to the fixing oar of Mixing Brush and rotating shaft be fixed better, described coupling shaft is horizontally disposed with equally spacedly along the axial both sides of rotating shaft, and symmetrically.
Wherein, in order to improve toughness and the intensity of industrial filter cloth film, the one of described industrial filter cloth film preferably in terylene short fiber filter cloth film, the long fine filter cloth film of terylene, polyvinyl filter cloth film, polypropylene fibre filter cloth film, the aperture of industrial filter cloth film is 1-100 μm.
In order to control the aeration rate of Aerobic Pond, spinner-type flowmeter is set in aeration tube.
Beneficial effect:
1, the flowing of sewage between the body of each pond all adopts from stream mode, waste water is after the first anaerobic pond anaerobic biological treatment, by the industrial filter cloth film solid-liquid separation between the first anaerobic pond and the first Aerobic Pond, after one-level anaerobic treatment, clear liquid is from flowing into the first Aerobic Pond, after the organic pollutant that aerobic microbiological effect in it is removed in sewage, by the industrial filter cloth film solid-liquid separation between the first good oxygen pond and the second anaerobic pond, after one-level aerobic treatment, clear liquid is from flowing into the second anaerobic pond, after the further anaerobic treatment of anaerobe in it, solid-liquid separation is carried out by the industrial filter cloth film between the second anaerobic pond and the second Aerobic Pond, clear liquid after secondary anaerobic process flows into the second Aerobic Pond, after in it, the organic pollutant in sewage is removed in aerobic microbiological effect further, solid-liquid separation is carried out by the industrial filter cloth film between the second Aerobic Pond and clear liquid storage pool, after one-level aerobic treatment, clear liquid enters clear liquid storage pool, discharge from water port, thus, have simple to operate, the feature of convenient management.
2, this device is the integrated device of anerobic-aerobic-anerobic-aerobe sewage treatment process, utilize pond body wall altogether, by industrial filter cloth film, the first anaerobic pond, the first Aerobic Pond, the second anaerobic pond and the second Aerobic Pond and clear liquid storage pool are separated, building together is an entirety, greatly reduces floor space and the scale of investment of combined treatment device.
3, adopt industrial filter cloth film to replace existing settling tank, economized sludge recirculation system, decreased facility investment, and saved land area further.
4, the whipping appts of band hairbrush is set in anaerobic pond, not only improve anaerobic sludge digestion efficiency, eliminate the layering of mud and waste water, increase the contact of mud and microorganism, and avoid in membrane filtration processes, colloid in solution and suspended particle are trapped under the effect of filter pressure thus exceedingly adsorption film is surperficial, cause membrane flux sharply to decline, and on the other hand, the colloid on film surface and suspended particle its composition and thickness in filtration procedure are changed along with the change of different processing requirement conditions, a kind of Dynamic Membrane can be formed.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
In order to deepen understanding of the present utility model, below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, and this embodiment, only for explaining the utility model, does not form the restriction to the utility model protection domain.
Shown in Figure 1, a kind of anaerobic-aerobic integrated waste disposal plant, comprise treatment tank, 4 pieces of industrial filter cloth films 1 are vertically set in treatment tank, treatment tank is separated into 5 parts, respectively be the first Aerobic Pond 2, first anaerobic pond 3, second Aerobic Pond 4, second anaerobic pond 5 and clear liquid storage pool 6, sludge discharging port 7 is all established in 2 described Aerobic Ponds and 2 anaerobic pond bottoms, first Aerobic Pond top is provided with fluid inlet 8, clear liquid storage pool bottom is provided with liquid outlet 9, the aeration tube 10 of multiple solarization air cap is provided with bottom first Aerobic Pond 2 and the second Aerobic Pond 4, described aeration tube stretches out outside Aerobic Pond along Aerobic Pond sidewall and is connected with the air compressor 11 being arranged on Aerobic Pond outside, in order to control the aeration rate of Aerobic Pond, spinner-type flowmeter 16 is set in aeration tube, in first anaerobic pond 3 and the second anaerobic pond 5, a grade whipping appts is set, described whipping appts comprises the Mixing Brush of the rotating shaft 12 be connected with motor 17 and the both sides being symmetricly set on rotating shaft, described Mixing Brush is made up of with the V-type bristle 14 being fixed on fixing oar both sides the fixing oar 13 vertically arranged, in order to promote the contact of mud and microorganism further, take away under the effect of filter pressure, be trapped within industrial filter cloth film surface colloid and suspended particle, the V-type of described V-type bristle is opening up, is preferably made by steel wire, copper wire or nylon material, described fixing oar 13 is connected with rotating shaft 12 by multiple coupling shaft 15, and in order to be fixed with rotating shaft 15 by the fixing oar 13 of Mixing Brush better, described coupling shaft is horizontally disposed with equally spacedly along the axial both sides of rotating shaft, and symmetrically.
Wherein, in order to improve toughness and the intensity of industrial filter cloth film, described industrial filter cloth film is preferably a kind of in terylene short fiber filter cloth film, the long fine filter cloth film of terylene, polyvinyl filter cloth film, polypropylene fibre filter cloth film, the preferred 1-100 μm in aperture of industrial filter cloth film.
Waste water enters the first anaerobic pond 2, the first anaerobic pond 2 is entered by the solarization air cap on aeration tube in the first anaerobic pond through air compressor 11 air blast, spinner-type flowmeter 16 aeration rate processed, after anaerobic biological treatment, spoil disposal bottom first anaerobic pond, by the clear liquid after the industrial filter cloth film solid-liquid separation between the first anaerobic pond and the first Aerobic Pond from flowing into the first Aerobic Pond 3, under stirring, after the organic pollutant that aerobic microbiological effect in it is removed in sewage, by the clear liquid after the industrial filter cloth film solid-liquid separation between the first good oxygen pond and the second anaerobic pond from flowing into the second anaerobic pond 4, similarly, the second anaerobic pond 4 is entered by the solarization air cap on aeration tube in the first anaerobic pond through air compressor air blast, spinner-type flowmeter controls aeration rate, after the further anaerobic treatment of anaerobe in it, the second Aerobic Pond 5 is flowed into by the clear liquid of the industrial filter cloth film solid-liquid separation between the second anaerobic pond and the second Aerobic Pond, under stirring, after in it, the organic pollutant in sewage is removed in aerobic microbiological effect further, clear liquid storage pool 6 is entered by the clear liquid after the industrial filter cloth film between the second Aerobic Pond and clear liquid storage pool carries out solid-liquid separation, discharge from water port.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (7)
1. an anaerobic-aerobic integrated waste disposal plant, it is characterized in that, comprise treatment tank, 4 pieces of industrial filter cloth films are vertically set in treatment tank, treatment tank is separated into 5 parts, respectively be the first Aerobic Pond, first anaerobic pond, second Aerobic Pond, second anaerobic pond and clear liquid storage pool, sludge discharging port is all established in 2 described Aerobic Ponds and 2 anaerobic pond bottoms, first Aerobic Pond top is provided with fluid inlet, clear liquid storage pool bottom is provided with liquid outlet, the aeration tube of multiple solarization air cap is provided with bottom first Aerobic Pond and the second Aerobic Pond, described aeration tube stretches out outside Aerobic Pond along Aerobic Pond sidewall and is connected with the air compressor being arranged on Aerobic Pond outside, in first anaerobic pond and the second anaerobic pond, whipping appts is set, described whipping appts comprises the Mixing Brush of the rotating shaft be connected with motor and the both sides being symmetricly set on rotating shaft, Mixing Brush is made up of the fixing oar vertically arranged and the V-type bristle being fixed on fixing oar both sides, fixing oar is connected with rotating shaft by multiple coupling shaft.
2. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1, is characterized in that the V-type of described V-type bristle is opening up.
3. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1 and 2, is characterized in that, described V-type bristle is made by steel wire, copper wire or nylon material.
4. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1, is characterized in that, described coupling shaft is horizontally disposed with equally spacedly along the axial both sides of rotating shaft, and symmetrically.
5. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1, is characterized in that, described industrial filter cloth film is selected from the one in terylene short fiber filter cloth film, the long fine filter cloth film of terylene, polyvinyl filter cloth film, polypropylene fibre filter cloth film.
6. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1 or 5, it is characterized in that, the aperture of described industrial filter cloth film is 1-100 μm.
7. a kind of anaerobic-aerobic integrated waste disposal plant according to claim 1, is characterized in that, in aeration tube, arrange spinner-type flowmeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520636179.XU CN205061690U (en) | 2015-08-21 | 2015-08-21 | Anaerobism - good oxygen integrative sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520636179.XU CN205061690U (en) | 2015-08-21 | 2015-08-21 | Anaerobism - good oxygen integrative sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061690U true CN205061690U (en) | 2016-03-02 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520636179.XU Expired - Fee Related CN205061690U (en) | 2015-08-21 | 2015-08-21 | Anaerobism - good oxygen integrative sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061690U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152331A (en) * | 2015-08-21 | 2015-12-16 | 南京白云化工环境监测有限公司 | Anaerobic-aerobic integrated sewage treatment device |
| CN109467187A (en) * | 2018-12-06 | 2019-03-15 | 中国科学院合肥物质科学研究院 | Waste water treatment system and its treatment process for high concentration antibiotic production wastewater |
| CN110902830A (en) * | 2019-12-10 | 2020-03-24 | 重庆振冉环保技术开发有限公司 | Integrated sewage treatment equipment |
-
2015
- 2015-08-21 CN CN201520636179.XU patent/CN205061690U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152331A (en) * | 2015-08-21 | 2015-12-16 | 南京白云化工环境监测有限公司 | Anaerobic-aerobic integrated sewage treatment device |
| CN105152331B (en) * | 2015-08-21 | 2018-03-13 | 南京白云化工环境监测有限公司 | A kind of anaerobic aerobic integratedization sewage-treatment plant |
| CN109467187A (en) * | 2018-12-06 | 2019-03-15 | 中国科学院合肥物质科学研究院 | Waste water treatment system and its treatment process for high concentration antibiotic production wastewater |
| CN110902830A (en) * | 2019-12-10 | 2020-03-24 | 重庆振冉环保技术开发有限公司 | Integrated sewage treatment equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160302 Termination date: 20180821 |