CN109320006A - A kind of black-odor riverway processing system - Google Patents
A kind of black-odor riverway processing system Download PDFInfo
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- CN109320006A CN109320006A CN201811047828.7A CN201811047828A CN109320006A CN 109320006 A CN109320006 A CN 109320006A CN 201811047828 A CN201811047828 A CN 201811047828A CN 109320006 A CN109320006 A CN 109320006A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0225—Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
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- 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
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Water Treatment By Sorption (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention reside in provide a kind of black-odor riverway processing unit, biology in the prior art is given full play to inhale phosphorus, release phosphorus principle, primary filter adsorption tank is set, after pollutant in sewage is carried out primary filtration, it uses with zeolite and active carbon as main adsorbing medium, the ammonia nitrogen in black and odorous water can be fully absorbed, and string bag filler is exchanged for by mechanical arm, while realizing sustainable progress, the filler for being adsorbed with a large amount of ammonia nitrogens can also be made full use of, biological treatment and physisorption are rationally utilized, black-odor riverway is handled, achieves good treatment effect.
Description
Technical field
The present invention relates to river water body pollution control fields, and in particular to a kind of river black and odorous water fast purification device.
Background technique
The quality of water environment improvement techniques system of black-odor riverway includes that dirt, purification of water quality, restoration of the ecosystem are cut in control source.Black smelly water
Body water correction technology mainly includes reoxygenation technology, flocculation, microbial bacterial agent technology, biology/ecological technique, ecological purification water factory
Etc. technologies etc..In the prior art for the technology of polluted river channel water body treating there are treatment cost height, engineering is huge, cost compared with
Height, regulation effect is poor, and purifying water body effect is ideal not to the utmost, needs to combine the technical problems such as other methods purifying water body water quality.
And it is common form that currently used ecological slope protection technology, which carries out in-situ treatment to black-odor riverway, such as using soil
Work Material cladding planting matrix, wire netting and rubble aggregate species phytyl, earth working material consolidate soil species phytyl, vegetation type eco-concrete,
Cement ecological planting matrix and soil-solidified-agent etc. carry out slope protection to riverbank, side slope, have better effects to stable bank slope structure, and
And certain improvement has been carried out to bank slope landscape, but it is very limited to the effect of retention face source pollutants discharged into rivers, and organic gel
It is so high to tie material cost, carries out construction on the spot and construction volume is also very big, popularization and use are restricted.
Summary of the invention
In order to solve the problems existing in the prior art, the present invention provides a kind of black-odor riverway processing unit.
Technical solution provided by the invention is as follows:
A kind of river black and odorous water processing unit, described device is arranged on river bank slope, if including standing on bank slope
Dry riser leans against the inclined plate that bank is broken, if the riser and inclined plate constitute filler stem pond, the filler pond is on bank slope from height
To low setting, the filler pond includes shell, and positioned at the water flow purification channel of interior of shell；The filler pond is from low to high
It is provided with primary filter adsorption tank 6, recovery of nitrogen and phosphorus adsorption tank 5, membrane filtration anaerobic pond 4, aerobic tank 3, anoxic pond 2 and anaerobic pond 1, institute
Shell one end is stated equipped with water inlet, the other end is equipped with water outlet, and water inlet and water outlet form water stream channel, the primary filter
Adsorption tank 6 is provided with river water inlet, and the water in black and odorous water enters primary filter adsorption tank 6 from the river water inlet, through first
For the water of grade filtering adsorption tank filtering by Pipeline transport into anaerobic pond 1, the water outlet in anaerobic pond 1 sequentially enters anoxic pond 2, good
Oxygen pond 3, membrane filtration anaerobic pond 4 and recovery of nitrogen and phosphorus adsorption tank 5, the water outlet of recovery of nitrogen and phosphorus adsorption tank 5 are directly discharged to river.
Further, in the aerobic tank be arranged aeration oxygen replenishing unit, the aeration oxygen replenishing unit close to the shell into
The mouth of a river, the aeration oxygen replenishing unit are nano bubble oxidation units.
Further, the aeration oxygen replenishing unit includes blower, automatic aerator and valve.
Further, the filler pond includes bacteria agent automatic adding device and the indoor filler of filler.
Further, the nano bubble oxidation unit includes nozzle, immersible pump, suction pipe, filter screen, control.
Further, the filler chamber is made of anti-corrosion material, and the filler chamber is the cabinet with reticulated cell, the filler
Room is fixedly mounted inside the housing.
Further, filler is placed in the filler chamber, multilayered structure is arranged in the primary filter adsorption tank, and water inlet first passes through
It crosses primary strainer the bulk materials in water body are trapped in water body, 3 layers of aperture are arranged from outside to inside successively in the primary strainer
Reduced strainer is provided with modularization filler in the strainer, and the modularization filler is by zeolite and active carbon according to 1-5:1
Ratio be filled in the string bag filler in the string bag, the string bag filler setting mechanical arm is picked up.
Further, it is added with porous aggregate in the recovery of nitrogen and phosphorus adsorption tank 5, and is arranged in recovery of nitrogen and phosphorus adsorption tank
There is dosing mouth, be added by dosing mouth and contain magnesium solution, the magnesium solution that contains is magnesium chloride solution, seawater, bittern or ashes solution
One of or it is a variety of；
Further, it after the string bag filler is picked up by mechanical arm, is added in recovery of nitrogen and phosphorus adsorption tank；
Further, the membrane filtration anaerobic pond uses Dual-layer structure, and top is membrane-filtering unit, and lower part is anaerobic zone, aerobic
Sludge in pond 3 is entered by pipeline from portion of membrane filtration anaerobic pond area, anaerobic reaction occurs in anaerobism bottom of pond portion, anaerobic reaction produces water row
Enter in recovery of nitrogen and phosphorus adsorption tank 5, aerobic tank water outlet enters membrane-filtering unit, and through membrane-filtering unit, treated that water is directly discharged in river；
Further, the aerobic tank 3 is provided with device for separating mud and water；
Further, what is filled in the recovery of nitrogen and phosphorus adsorption tank is granular pattern compound adsorbent, and the granular pattern is multiple
Closing adsorbent is to prepare in accordance with the following steps:
1) phosphorus containing sludge is subjected to sludge dewatering, obtains dewatered sludge；Dewatered sludge is subjected to broken wall treatment, the broken wall
Processing is carried out using supersonic wave wall breaking, high steam broken wall or high pressure fracture broken wall mode, and the mixture after broken wall is passed through point
It is separated by solid-liquid separation from device, obtains solid matter and liquid；
2) fast pyrogenation is carried out to generate pyrolysis gas and charcoal, to pyrolysis to the solid matter using about 680 DEG C of temperature
Gas is recycled or is further processed；
Preferably, crop material is mixed into before pyrolysis in the solid matter, the crop material carries out before being mixed into
It air-dries, break process, partial size is 1cm hereinafter, mixed volume ratio is solid matter: stalk=2-6:3-8；
3) Modified Activated Carbon is mixed with iron filings according to a certain percentage, the iron filings mass fraction is 20-40%, described to change
Property charcoal mass fraction be 60-80%, prepare granular pattern compound adsorbent.
It further, further include integrated control device, the integrated control device includes switch control module, time control
Module, Wireless-wire control module, Internet of Things control module.
Compared with prior art, the beneficial effects of the present invention are:
1, the present invention gives full play to biology in the prior art and inhales phosphorus, releases phosphorus principle, primary filter adsorption tank is arranged, by sewage
In pollutant carry out primary filtration after, use with zeolite and active carbon as main adsorbing medium, black smelly water can be fully absorbed
Ammonia nitrogen in body, and exchanged for string bag filler by mechanical arm, while realizing sustainable progress, it can also make full use of
It is adsorbed with the filler of a large amount of ammonia nitrogens；
2, the present invention in granular pattern compound adsorbent preparation, prepare height using the excess sludge in sewage disposal process
The charcoal of adsorption capacity, using phosphorus containing sludge raw material the most, in carbonisation, phosphorus therein can be attached directly in charcoal hole,
In the reaction of subsequent guanite, what struvite production can be more firm is attached in charcoal hole, further promotes guanite sustained release effect
Fruit can prepare controlled availability fertilizer；
3, the present invention has efficient removal ability to COD, nitrogen, phosphorus in black and odorous water, and it is black smelly can to substantially reduce river
The pollution level of water body.
In addition, carrying out simple modifications to existing waterway, the reluctant defect in existing waterway is not only solved, can also be filled
Divide nitrogen phosphorus in recycling black and odorous water, and prepares the slow release fertilizer rich in organic matter, nitrogen phosphorus that can be applied in soil.
Detailed description of the invention
Fig. 1 is a kind of black-odor riverway processing unit schematic diagram of the present invention；
Specific embodiment
In order to be best understood from the present invention, the present invention is described in further detail below in conjunction with the drawings and specific embodiments.
Embodiment 1
As shown in Figure 1, for river black and odorous water fast purification device in the present embodiment, a kind of river black and odorous water processing dress
Set, described device is arranged on river bank slope, including stand several risers on bank slope, lean against bank it is broken on inclined plate, it is described
If riser and inclined plate constitute filler stem pond, from up to low setting on bank slope, the filler pond includes shell in the filler pond, with
And the water flow purification channel positioned at interior of shell；The filler pond is provided with primary filter adsorption tank 6, recovery of nitrogen and phosphorus from low to high
Adsorption tank 5, membrane filtration anaerobic pond 4, aerobic tank 3, anoxic pond 2 and anaerobic pond 1, described shell one end are equipped with water inlet, and the other end is set
There is water outlet, water inlet and water outlet form water stream channel, and the primary filter adsorption tank 6 is provided with river water inlet, black smelly
Water in water body enters primary filter adsorption tank 6 from the river water inlet, and the water filtered through primary filter adsorption tank passes through pipeline
It is delivered in anaerobic pond 1, the water outlet in anaerobic pond 1 sequentially enters anoxic pond 2, aerobic tank 3, membrane filtration anaerobic pond 4 and recovery of nitrogen and phosphorus
The water outlet of adsorption tank 5, recovery of nitrogen and phosphorus adsorption tank 5 is directly discharged to river.
In the present embodiment, aeration oxygen replenishing unit is set in the aerobic tank, and the aeration oxygen replenishing unit is close to described outer
Shell water inlet, the aeration oxygen replenishing unit are nano bubble oxidation units.The nano bubble oxidation unit includes nozzle, diving
Pump, suction pipe, filter screen, control cabinet.
In the present embodiment, 1 material of shell uses corrosion-resistant engineering plastics, stainless steel or glass reinforced plastic.
In the present embodiment, a kind of river black and odorous water fast purification device further includes integrated control device, described
Integrated control device includes switch control module, time control module, Wireless-wire control module, Internet of Things control module.
In the present embodiment, the bubble diameter that the nano bubble oxidation unit generates is at 0.3~3 micron.
In the present embodiment, filler is placed in the filler chamber, multilayered structure, water inlet is arranged in the primary filter adsorption tank
It first passes through primary strainer the bulk materials in water body are trapped in water body, 3 layers of aperture are arranged from outside to inside in the primary strainer
The strainer successively reduced, is provided with modularization filler in the strainer, the modularization filler be by zeolite and active carbon according to
The ratio of 1-5:1 is filled in the string bag filler in the string bag, and the string bag filler setting mechanical arm is picked up.
In the present embodiment, porous aggregate is added in the recovery of nitrogen and phosphorus adsorption tank 5, and in recovery of nitrogen and phosphorus adsorption tank
It is provided with dosing mouth, is added by dosing mouth and contains magnesium solution, the magnesium solution that contains is magnesium chloride solution, seawater, bittern or ashes
One of solution is a variety of；
In the present embodiment, the membrane filtration anaerobic pond uses Dual-layer structure, and top is membrane-filtering unit, and lower part is anaerobism
Area, the sludge in aerobic tank 3 are entered by pipeline from portion of membrane filtration anaerobic pond area, and anaerobic reaction, anaerobism occurs in anaerobism bottom of pond portion
Reaction produces water and is discharged into recovery of nitrogen and phosphorus adsorption tank 5, and aerobic tank water outlet enters membrane-filtering unit, and through membrane-filtering unit, treated that water is direct
It is emitted into river.
Table 1 is to run water quality monitoring result using the present embodiment:
According to above-mentioned collection result it is found that scene examines on the spot, the river and downstream after using apparatus of the present invention 90 days
Water quality is obviously improved, black smelly elimination, colorless and odorless, and transparency increases obviously, and river is eliminated by bank black mud, is swum in water body dynamic
Object, fish increase, and water body purification effect is obvious.
Embodiment 2
It improves on the basis of embodiment 1, what is filled in the recovery of nitrogen and phosphorus adsorption tank is the compound suction of granular pattern
Attached dose, the granular pattern compound adsorbent is to prepare in accordance with the following steps:
1) phosphorus containing sludge is subjected to sludge dewatering, obtains dewatered sludge；Dewatered sludge is subjected to broken wall treatment, the broken wall
Processing is carried out using supersonic wave wall breaking, high steam broken wall or high pressure fracture broken wall mode, and the mixture after broken wall is passed through point
It is separated by solid-liquid separation from device, obtains solid matter and liquid；
2) fast pyrogenation is carried out to generate pyrolysis gas and charcoal, to pyrolysis to the solid matter using about 670 DEG C of temperature
Gas is recycled or is further processed；
Preferably, crop material is mixed into before pyrolysis in the solid matter, the crop material carries out before being mixed into
It air-dries, break process, partial size is 1cm hereinafter, mixed volume ratio is solid matter: stalk=5:5；
3) Modified Activated Carbon is mixed with iron filings according to a certain percentage, the iron filings mass fraction is 40%, the modification
Charcoal mass fraction is 60%, prepares granular pattern compound adsorbent.
In the present embodiment, the water in recovery of nitrogen and phosphorus adsorption tank is aerated using aerator, wherein aerating gas
For carbon dioxide gas, calcium carbonate layer is arranged in the aerator top.
Embodiments of the present invention and embodiment are not limited to the above, and above content according to the invention utilizes ability
The ordinary technical knowledge and customary means in domain, under the premise of not departing from above-mentioned basic fundamental thought of the invention, the present invention can be with
The modification, replacement or change for making other diversified forms, all fall within rights protection scope of the present invention.
Claims (10)
1. a kind of black-odor riverway processing unit, which is characterized in that described device is arranged on river bank slope, including stands on bank slope
Several risers, lean against bank it is broken on inclined plate, if the riser and inclined plate constitute filler stem pond, the filler pond is on bank slope
From up to low setting, the filler pond includes shell, and positioned at the water flow purification channel of interior of shell；The filler pond is by low
There are primary filter adsorption tank, recovery of nitrogen and phosphorus adsorption tank, membrane filtration anaerobic pond, aerobic tank, anoxic pond and anaerobic pond to high setting, it is described
Shell one end is equipped with water inlet, and the other end is equipped with water outlet, and water inlet and water outlet form water stream channel, and the primary filter is inhaled
Attached pond is provided with river water inlet, and the water in black and odorous water enters primary filter adsorption tank from the river water inlet, through primary mistake
The water for filtering adsorption tank filtering passes through Pipeline transport into anaerobic pond, and the water outlet in anaerobic pond sequentially enters anoxic pond, aerobic tank, film
Filter anaerobic pond and recovery of nitrogen and phosphorus adsorption tank, the water outlet of recovery of nitrogen and phosphorus adsorption tank are directly discharged to river.
2. device as described in claim 1, which is characterized in that place filler, the primary filter absorption in the filler chamber
Multilayered structure is arranged in pond, and water inlet first passes through primary strainer and the bulk materials in water body are trapped in water body, the primary strainer
The strainer that 3 layers of aperture successively reduce from outside to inside is set, modularization filler is provided in the strainer, the modularization filler is
Zeolite and active carbon are filled in the string bag filler in the string bag according to the ratio of 1-5:1, the string bag filler be arranged mechanical arm into
Row picks up.
3. device as described in claim 1, which is characterized in that porous aggregate is added in the recovery of nitrogen and phosphorus adsorption tank, and
It is provided with dosing mouth in recovery of nitrogen and phosphorus adsorption tank, is added by dosing mouth and contains magnesium solution, it is described molten for magnesium chloride containing magnesium solution
One of liquid, seawater, bittern or ashes solution are a variety of.
4. device as described in claim 1, which is characterized in that the membrane filtration anaerobic pond uses Dual-layer structure, and top is
Membrane-filtering unit, lower part are anaerobic zone, and the sludge in aerobic tank is entered by pipeline from portion of membrane filtration anaerobic pond area, in anaerobism bottom of pond portion
Anaerobic reaction occurs, anaerobic reaction produces water and is discharged into recovery of nitrogen and phosphorus adsorption tank, and aerobic tank water outlet enters membrane-filtering unit, fills through membrane filtration
Setting treated, water is directly discharged in river.
5. device as described in claim 1, which is characterized in that is filled in the recovery of nitrogen and phosphorus adsorption tank is that granular pattern is multiple
Close adsorbent.
6. device as described in claim 1, which is characterized in that is filled in the recovery of nitrogen and phosphorus adsorption tank is that granular pattern is multiple
Close adsorbent.
7. device as described in claim 1, which is characterized in that it further include integrated control device, the integrated control device packet
Include switch control module, time control module, Wireless-wire control module, Internet of Things control module.
8. device as described in claim 1, which is characterized in that aeration oxygen replenishing unit, the aeration are arranged in the aerobic tank
Oxygenation unit is nano bubble oxidation unit close to the shell water inlet, the aeration oxygen replenishing unit.
9. device as described in claim 1, which is characterized in that the filler pond include bacteria agent automatic adding device and
The indoor filler of filler.
10. device as described in claim 1, which is characterized in that after the string bag filler is picked up by mechanical arm, add
Into recovery of nitrogen and phosphorus adsorption tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811047828.7A CN109320006B (en) | 2018-09-10 | 2018-09-10 | Black and odorous river course processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811047828.7A CN109320006B (en) | 2018-09-10 | 2018-09-10 | Black and odorous river course processing system |
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| Publication Number | Publication Date |
|---|---|
| CN109320006A true CN109320006A (en) | 2019-02-12 |
| CN109320006B CN109320006B (en) | 2023-09-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811047828.7A Active CN109320006B (en) | 2018-09-10 | 2018-09-10 | Black and odorous river course processing system |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1000904A2 (en) * | 1998-11-11 | 2000-05-17 | Mitsubishi Materials Corporation | Method for recovering phosphate from sludge and system therefor |
| CN103373793A (en) * | 2012-04-27 | 2013-10-30 | 中国科学院城市环境研究所 | High-efficiency and low-consumption livestock and poultry breeding wastewater treatment and recycling technology |
| CN104773897A (en) * | 2014-01-13 | 2015-07-15 | 中国科学院烟台海岸带研究所 | Coast lack-odor river channel water quality in-situ remediation system |
| CN105174463A (en) * | 2015-10-20 | 2015-12-23 | 中国科学院重庆绿色智能技术研究院 | Sewage treatment system and method based on sludge carbon source and nitrogen and phosphorus recycling |
| CN206203981U (en) * | 2016-09-26 | 2017-05-31 | 深圳市铁汉生态环境股份有限公司 | A kind of revetment ramp type bio-contact oxidation system |
| CN107673561A (en) * | 2017-11-07 | 2018-02-09 | 中交生态环保投资有限公司 | A kind of black and odorous water in-situ treatment system and processing method |
-
2018
- 2018-09-10 CN CN201811047828.7A patent/CN109320006B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1000904A2 (en) * | 1998-11-11 | 2000-05-17 | Mitsubishi Materials Corporation | Method for recovering phosphate from sludge and system therefor |
| CN103373793A (en) * | 2012-04-27 | 2013-10-30 | 中国科学院城市环境研究所 | High-efficiency and low-consumption livestock and poultry breeding wastewater treatment and recycling technology |
| CN104773897A (en) * | 2014-01-13 | 2015-07-15 | 中国科学院烟台海岸带研究所 | Coast lack-odor river channel water quality in-situ remediation system |
| CN105174463A (en) * | 2015-10-20 | 2015-12-23 | 中国科学院重庆绿色智能技术研究院 | Sewage treatment system and method based on sludge carbon source and nitrogen and phosphorus recycling |
| CN206203981U (en) * | 2016-09-26 | 2017-05-31 | 深圳市铁汉生态环境股份有限公司 | A kind of revetment ramp type bio-contact oxidation system |
| CN107673561A (en) * | 2017-11-07 | 2018-02-09 | 中交生态环保投资有限公司 | A kind of black and odorous water in-situ treatment system and processing method |
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| Publication number | Publication date |
|---|---|
| CN109320006B (en) | 2023-09-15 |
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