CN110054347A - A kind of pollution of river object Integrated Processing Unit - Google Patents
A kind of pollution of river object Integrated Processing Unit Download PDFInfo
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- CN110054347A CN110054347A CN201910225225.XA CN201910225225A CN110054347A CN 110054347 A CN110054347 A CN 110054347A CN 201910225225 A CN201910225225 A CN 201910225225A CN 110054347 A CN110054347 A CN 110054347A
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- river
- processing unit
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- 238000012545 processing Methods 0.000 title claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims abstract description 71
- 230000003647 oxidation Effects 0.000 claims abstract description 40
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 40
- 210000005239 tubule Anatomy 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 238000007747 plating Methods 0.000 claims description 8
- 230000002906 microbiologic effect Effects 0.000 claims description 7
- 238000012856 packing Methods 0.000 claims description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 239000010936 titanium Substances 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 201000002282 venous insufficiency Diseases 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 229910002804 graphite Inorganic materials 0.000 claims description 3
- 239000010439 graphite Substances 0.000 claims description 3
- 239000007769 metal material Substances 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 229910000914 Mn alloy Inorganic materials 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims 1
- 238000006731 degradation reaction Methods 0.000 abstract description 18
- 230000015556 catabolic process Effects 0.000 abstract description 16
- 239000003344 environmental pollutant Substances 0.000 abstract description 10
- 231100000719 pollutant Toxicity 0.000 abstract description 10
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 41
- 239000000243 solution Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 238000007667 floating Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000002957 persistent organic pollutant Substances 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000003403 water pollutant Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000001684 chronic effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- -1 ecological method) Chemical compound 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000007954 hypoxia Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 239000003621 irrigation water Substances 0.000 description 1
- 210000000867 larynx Anatomy 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000013033 photocatalytic degradation reaction Methods 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- 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
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
-
- 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
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- 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
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
-
- 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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
- Physical Water Treatments (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a kind of pollution of river object Integrated Processing Units, it include: the reaction tube of the first raft, the second raft and hanging below two rafts, inside reaction tube, along the axial direction of reaction tube, it is disposed with a pair of of electrocatalytic oxidation pole plate, trunnion, two pieces of ultraviolet lamp plates, aerobic reaction section and electronic rotating vane.Apparatus of the present invention provide electric power using solar energy and battery, it is not necessary that power device is additionally arranged, it can be realized as handling the round-the-clock of pollution of river object incessantly, and, apparatus of the present invention both can effective degradation of organic substances, the nutriments such as nitrogen phosphorus can be handled well again, be particularly suitable for the comprehensive treatment in the river of pollutant complexity.
Description
Technical field
The invention belongs to technical field of sewage in environmental protection, and in particular to a kind of pollution of river object integrated treatment dress
It sets.
Background technique
With the fast development of Chinese economy, China's water environmental problems become increasingly conspicuous, town and country water environment suffers from unprecedented
It threatens.China's municipal wastewater centralized treatment rate is only 13.4%, compared with developed country wastewater treatment rate 80%-90%, China
Wastewater treatment rate is extremely low, and a large amount of raw sewerages are directly discharged into rivers, causes the serious pollution of river water quality.Chemical fertilizer and agriculture
The excessive application of medicine causes a large amount of chemical fertilizer, pesticide to flow into river with precipitation or irrigation water, also becomes important pollution sources.Area
Economic extensive production mode not yet changes, and technology falls behind, and the indexs such as the low material consumption of efficiency of energy utilization, energy consumption occupy height not
Under.Economic growth is exchanged for sacrificialing environment and resource, is the immanent cause that river pollution is got worse.There is investigation to show the Changjiang river
90% or more Delta Area Rural Water Environment ecology has lost basic function, because pollution and the ecosystem are seriously degenerated, city
Township's river water quality has been substantially at V class and bad V class water quality, and most river water bodies are seriously polluted, eutrophication, and water hypoxia becomes
Blacking is smelly, causes severe Environmental situations.
Currently, the polluted river channel Treatment process used both at home and abroad specifically includes that physical method, such as dredging, mechanical algae removement, diversion
Dilution, artificial flowing, aeration etc.；The precipitating that molysite promotes phosphorus is added if chemical reagent removes algae in chemical method, and lime denitrogenation is added
Deng；Bioanalysis, such as artificial wetland treatment, hydrophyte restoration, microorganism remediation and biological floating bed.These single processing sides
Method cuts both ways, for example, some methods can only handle the nutriments such as nitrogen phosphorus (such as ecological method), some methods can only be to organic
Object carries out oxidative degradation (such as photocatalytic degradation method), for polluted river channel, since many years chronic pollution leads to its ecosystem
Structure is seriously destroyed, and cannot solve environmental problem at all by single processing method merely, and should design a kind of can be handled simultaneously
The device of multiple pollutant constructs the aquatic ecosystem of benign cycle, and reaching fundamentally improves water quality, improves self-purification of water energy
The purpose of power.
Summary of the invention
In view of this, can either degrade has the purpose of the present invention is to provide a kind of pollution of river object Integrated Processing Unit
Machine object, and be capable of handling the nutriments such as nitrogen phosphorus, the device can not be subject to seasonal restrictions round-the-clock place without power, non-maintaining
Multiple pollutant is managed, realizes the comprehensive treatment of the river water body for pollutant complexity.
A kind of pollution of river object Integrated Processing Unit, comprising:
First raft, first raft includes the first battery and the first cavity, in first floating
The first solar panel is additionally provided on platform；
Second raft, second raft includes the second battery and the second cavity, in second floating
The second solar panel is additionally provided on platform；
Reaction tube, the reaction pipe pendant is in the lower section of first raft and second raft, in institute
State inside reaction tube, along the axial direction of the reaction tube, be disposed with a pair of of electrocatalytic oxidation pole plate, trunnion, two pieces it is ultraviolet
Lamp plate, aerobic reaction section and electronic rotating vane, the electrocatalytic oxidation pole plate setting are flat in the reaction tube and first floating
One end of platform connection, place, the throat of the trunnion is equipped with upward tubule, and the top of the tubule is more than river surface, described in every piece
Ultraviolet lamp plate is respectively equipped with the quartz glass cover for surrounding it, and is coated with two on the intermediate setting surface of two pieces of ultraviolet lamp plates
The corrugated plating of titanium oxide catalyst, the aerobic reaction section refers to the biologic packing material that suspension is provided in this section of reaction tube, described
Biologic packing material area load has aerobic microbiological, and the electronic rotating vane setting connects in the reaction tube and second raft
The one end connect；
The electrocatalytic oxidation pole plate is connect with first battery, and the electronic rotating vane and second battery connect
It connects, the ultraviolet lamp plate is connect with first battery or second battery, by the first battery and the second battery
Electric power is provided for electrocatalytic oxidation pole plate, electronic rotating vane, ultraviolet lamp plate.
In preferred technical solution, the anode of the electrocatalytic oxidation pole plate is coating titanium anode, graphite electrode or lead
Mangonic electrode.
In preferred technical solution, the cathode of the electrocatalytic oxidation pole plate uses metal material, such as: titanium, stainless steel.
In preferred technical solution, the electrode spacing of the electrocatalytic oxidation pole plate is 40 centimetres.
In preferred technical solution, the inter-electrode voltage of the electrocatalytic oxidation pole plate is 3~10V DC voltage, most preferably
Voltage is 10V.
In preferred technical solution, the length of the aerobic reaction section is the 1/4~1/3 of the tube length of reaction tube.
In preferred technical solution, the diameter of the tubule is the 1/10~1/20 of the caliber of the reaction tube, to obtain
Better Venturi effect.
In preferred technical solution, the revolving speed of the electronic rotating vane is 50~300r/min, so that the water inside reaction tube
Flow velocity degree is about 10cm/min, to extend the reaction time that water pollutant is degraded in reaction tube, so that pollutant
It degrades more thorough.
In preferred technical solution, it is provided with constent temperature heater on the inner wall of the reaction tube, so that inside reaction tube
Temperature be maintained at 25~28 DEG C.
In preferred technical solution, downward pendant hypostasis is connected in the lower part of the reaction tube.
In preferred technical solution, the reaction tube is horizontal reaction tube.
When using apparatus of the present invention, device is placed in korneforos, the first raft and the second raft are bubbled through the water column,
It is suspended in the reaction tube below the first raft and the second raft to be placed among river, adjusts the first solar panel
With the direction of the second solar panel so that the first solar panel and the second solar panel face the sun towards south
Light, to receive more solar energy.
When sunlight irradiation, the first solar panel and the second solar panel collect solar energy, and by luminous energy
It is conveyed to the first battery and the second battery after being converted to electric energy, by the first battery and the second battery stores electricity energy.
After the first battery and the second battery have enough electric power, to electrocatalytic oxidation pole plate, electronic rotating vane and ultraviolet
Lamp plate provides electric power, and the power supply of electrocatalytic oxidation pole plate is switched on, and ultraviolet lamp plate is lit, and electronic rotating vane starts turning.
The rotation of electronic rotating vane will push water in reaction tube from one end close to electrocatalytic oxidation pole plate to close to electronic
The flowing of one end of rotating vane, it is final to flow out reaction tube and enter in river.
The process that water is flowed from one end close to electrocatalytic oxidation pole plate to one end close to electronic rotating vane in reaction tube
In, first pass around electrocatalytic oxidation pole plate, organic pollutants reaction of decomposing is decomposed；Then water can flow to larynx
Pipe, and water velocity is accelerated at the throat of trunnion, externally forms negative pressure, sucks air by tubule, increases water body dissolution
Oxygen, while minute bubbles are formed in water, due to being coated with catalyst, under ultraviolet light, organic contamination in water on corrugated plating
Object can degrade, and can promote electron transmission and separation in the minute bubbles that ripple plate surface is formed, and improve degradation speed；So
Afterwards, these minute bubbles can reach aerobic reaction section with water flow, therein when being contacted due to aerobic microbiological with water pollutant
Aerobic degradation occurs for the nutriments such as organic pollutant and nitrogen phosphorus, and minute bubbles have aerobic microbiological with the load wherein filled
The contact of biologic packing material surface when, can supplement Institute of Micro-biology needs air, enhances oxidability, improves the efficiency of aerobic degradation；Most
Afterwards, water outflows back in river from reaction tube close to one end of electronic rotating vane.Under the rotation of electronic rotating vane, water can be with dissolution
Oxygen be discharged into river and rise, achieve the purpose that recycle up and down, so that entire pollution of river object is gradually degraded, also achieve river
The integrated treatment of road pollutant.
Compared with prior art, the invention has the following beneficial technical effects:
1) apparatus of the present invention provide electric power using solar energy and battery, and power device is arranged without additional, it will be able to
Realization handles the round-the-clock of pollution of river object incessantly, either daytime or evening, winter or summer, completely not
It is influenced by season, weather and time, operating cost is low, easy maintenance low cost, applied widely；
2) apparatus of the present invention are provided with electrocatalysis oxidation apparatus, ultraviolet catalytic oxidation unit and aerobic degradation reaction section, both
Can effective degradation of organic substances, and the nutriments such as nitrogen phosphorus can be handled well, be particularly suitable for the river of pollutant complexity
Comprehensive treatment.
3) apparatus of the present invention can increase oxygen content by the setting of trunnion, both promote the catalytic degradation on corrugated plating,
Microorganism aerobic degradation is promoted again, and degradation efficiency greatly promotes, and treatment effect is very good；
4) in apparatus of the present invention electronic rotating vane setting, can either guarantee the slow flowing for reacting in-pipe flow, and can
Accelerate the circulation on river upper layer and bottom water body, so as to realize the integrated treatment to entire pollution of river object.
5) apparatus of the present invention structure is simple, and manufacture is easy, low in cost, easy to adjust, can be by adjusting aerobic reaction
The setting of the length, the length of ultraviolet lamp plate and electrocatalytic oxidation pole plate of section, adapts to the comprehensive of the pollution of river object of different quality
Conjunction processing.
These and other objects of the invention, feature and advantage, by following detailed descriptions, drawings and claims are obtained
To fully demonstrate, and can be achieved by means, device and the their combination specially pointed out in appended claims.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of a specific embodiment of pollution of river object Integrated Processing Unit of the invention.
Specific embodiment
Hereinafter, in conjunction with the accompanying drawings and embodiments, detailed description of embodiments of the present invention, to be more clearly understood that this
The technology contents of invention.
As shown in Figure 1, in a specific embodiment of the invention, a kind of pollution of river object Integrated Processing Unit, comprising:
First raft 1, the first raft 1 includes the first battery 2 and the first cavity 3, in the first raft 1
On be additionally provided with the first solar panel 4；
Second raft 1', the second raft 1' includes the second battery 2' and the second cavity 3', in the second floating
The second solar panel 4' is additionally provided on platform 1'；
Reaction tube 5, for the hanging of reaction tube 5 in the lower section of the first raft 1 and the second raft 1', reaction tube 5 is in water
Level state, along the axial direction of reaction tube 5, is disposed with a pair of of electrocatalytic oxidation pole plate 6, trunnion 7, two inside reaction tube 5
The ultraviolet lamp plate 9 of block, aerobic reaction section 11 and electronic rotating vane 12, the setting of electrocatalytic oxidation pole plate 6 are flat in reaction tube 5 and the first floating
One end that platform 1 connects, the throat of trunnion 7 locate (most narrow place) equipped with upward tubule 8, and the top of tubule 8 is more than river surface, and every piece
Ultraviolet lamp plate 9 has been separately equipped with a quartz glass cover, and ultraviolet lamp plate 9 is surrounded by quartz glass cover, and in two pieces of ultraviolet lamps
The intermediate setting surface of plate 9 is coated with the corrugated plating 10 of titanium deoxide catalyst, and aerobic reaction section 11 refers in this section of reaction tube
It is provided with the biologic packing material of suspension, biologic packing material area load has an aerobic microbiological, and the electronic setting of rotating vane 12 is in reaction tube 5 and the
One end of two raft 1' connections；
Electrocatalytic oxidation pole plate 6 is connect with the first battery 2, and electronic rotating vane 12 is connect with the second battery 2', ultraviolet lamp
Plate 9 is connect with the first battery 2 or the second battery 2'；It is electrocatalytic oxidation pole by the first battery 2 and the second battery 2'
Plate 6, electronic rotating vane 12, ultraviolet lamp plate 9 provide electric power.
The application method and working principle of pollution of river object Integrated Processing Unit in above-described embodiment are as follows:
In use, above-mentioned apparatus is placed in korneforos, the first raft 1 and the second raft 1' bubble through the water column, suspention
Reaction tube 5 below the first raft 1 and the second raft 1' is placed among river, adjusts the first solar panel
4 and second solar panel 4' direction so that the first solar panel 4 and the second solar panel 4' are towards southern face
Sunlight, to receive more solar energy
When sunlight irradiation, the first solar panel 4 and the second solar panel 4' collect solar energy, and by light
It is conveyed to the first battery 2 and the second battery 2' after electric energy can be converted to, is stored by the first battery 2 and the second battery 2'
Electric energy.
After the first battery 2 and the second battery 2' have enough electric power, electrocatalytic oxidation pole plate 6, electronic rotating vane 12 are given
Electric power is provided with ultraviolet lamp plate 9, the power supply of electrocatalytic oxidation pole plate 6 is switched on, and ultraviolet lamp plate 9 is lit, and electronic rotating vane 12 is opened
Begin to rotate.
The rotation of electronic rotating vane 12 will push water in reaction tube 5 from one end close to electrocatalytic oxidation pole plate 6 to close
The flowing of one end of electronic rotating vane 12, it is final to flow out reaction tube 5 and enter in river.
What water was flowed from one end close to electrocatalytic oxidation pole plate 6 to one end close to electronic rotating vane 12 in reaction tube 5
In the process, electrocatalytic oxidation pole plate 6 is first passed around, organic pollutants reaction of decomposing is decomposed；Then water can flow
To trunnion 7, and at the throat of trunnion 7, water velocity is accelerated, and externally forms negative pressure, sucks air by tubule 8, increases water
Body dissolved oxygen, while minute bubbles are formed in water, since 10 surface of corrugated plating is coated with catalyst, under ultraviolet light, water
Middle organic pollutant can degrade, and can promote electron transmission and separation in the minute bubbles that 10 surface of corrugated plating is formed, and improve
Degradation speed；Then, these minute bubbles can reach aerobic reaction section 11 with water flow, due to polluting in aerobic microbiological 11 and water
When object contacts, aerobic degradation occurs for the nutriments such as organic pollutant and nitrogen phosphorus therein, and minute bubbles with wherein fill
When load has the biologic packing material surface of aerobic microbiological to contact, can supplement Institute of Micro-biology needs air, enhances oxidability, improves
The efficiency of aerobic degradation；Finally, water outflows back in river from reaction tube 5 close to one end of electronic rotating vane 12.In electronic rotating vane
Under 12 rotation, water can be discharged into river with the oxygen of dissolution and rise, and achieve the purpose that recycle up and down, make the entire pollution of river
Object is gradually degraded, and also achieves the integrated treatment of pollution of river object.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, electricity
The anode of catalysis oxidation pole plate 6 can be coating titanium anode, graphite electrode or lead base manganese alloy electrode.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, electricity
The cathode of catalysis oxidation pole plate 6 can use common metal material, such as: titanium, stainless steel.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, it can
The electrode spacing (spacing of two-plate) of this pair of of electrocatalytic oxidation pole plate 6 is arranged as 40 centimetres.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, it can
The voltage between pole plate this pair of of electrocatalytic oxidation pole plate 6 is arranged is 3~10V DC voltage (that is, in electrocatalytic oxidation pole plate
Apply 3~10V DC voltage in 6 anode and cathode), optimum voltage 10V.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, it is good
The length of oxygen conversion zone 11 is the 1/4~1/3 of the length of reaction tube 5.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, carefully
The diameter of pipe 8 is the 1/10~1/20 of the caliber of reaction tube 5, to obtain better Venturi effect.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, electricity
The revolving speed of turn leaf 12 is 50~300r/min, so that the water velocity inside reaction tube 5 is about 10cm/min, to extend in water
The reaction time that pollutant is degraded in reaction tube 5, so that pollutant reaction and degradation are more thorough.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, also
Constent temperature heater can be set on the inner wall of reaction tube 5, so that the temperature inside reaction tube 5 is maintained at 25~28 DEG C, so that
Aerobic degradation it is more efficient.
It will be understood by those skilled in the art that in the specific embodiment of above-mentioned pollution of river object Integrated Processing Unit, also
Downward pendant hypostasis can be connected in the lower part of reaction tube 5.Pendant hypostasis can be concrete block or other weights.
In apparatus of the present invention, ultraviolet lamp plate can be ultraviolet LED lamp plate, usually be composed of more ultraviolet LED lamps
, it can be as needed by more commercially available ultraviolet LED lamps by constituting plate part after welding and assembling.
In apparatus of the present invention, the first battery and the second battery can be battery group, as needed, can install more
Group storage battery, or installing transformer.
A kind of pollution of river object Integrated Processing Unit of the above-mentioned apparatus as green, make full use of solar energy green energy resource and
The electric power storage of battery acts on, and power device is arranged without additional, it will be able to realize for the round-the-clock uninterrupted of pollution of river object
Ground processing, either daytime or evening, winter or summer, are not influenced completely by season, weather and time；Meanwhile it is logical
Setting gradually for electrocatalysis oxidation apparatus, ultraviolet catalytic oxidation unit and aerobic degradation reaction section is crossed, both can effectively degrade has
Machine object, and the nutriments such as nitrogen phosphorus can be handled well, it is particularly suitable for the comprehensive treatment in the river of pollutant complexity；And
And by the setting of trunnion, oxygen content can be increased, not only promoted the catalytic degradation on corrugated plating, but also to promote microorganism good
Oxygen degradation, degradation efficiency greatly promote, and treatment effect is very good；In addition, the setting of electronic rotating vane, can either guarantee in reaction tube
The slow flowing of water flow, and can speed up the circulation on river upper layer and bottom water body, so as to realize to the entire pollution of river
The integrated treatment of object.
It can be seen that the purpose of the present invention completely and is effectively achieved.Function and structural principle of the invention
It is shown and is illustrated in embodiment, without departing substantially from the principle, embodiment can make any modification.Institute
With present invention comprises all variant embodiments based on claim spirit and scope of the claims.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (10)
1. a kind of pollution of river object Integrated Processing Unit characterized by comprising
First raft, first raft includes the first battery and the first cavity, in first raft
On be additionally provided with the first solar panel；
Second raft, second raft includes the second battery and the second cavity, in second raft
On be additionally provided with the second solar panel；
Reaction tube, the reaction pipe pendant is in the lower section of first raft and second raft, described anti-
Should inside pipe, along the axial direction of the reaction tube, be disposed with a pair of of electrocatalytic oxidation pole plate, trunnion, two pieces of ultraviolet lamp plates,
Aerobic reaction section and electronic rotating vane, the electrocatalytic oxidation pole plate setting are connect in the reaction tube with first raft
One end, upward tubule is equipped at the throat of the trunnion, the top of the tubule is more than river surface, every piece of ultraviolet lamp
Plate is respectively equipped with the quartz glass cover for surrounding it, and is coated with titanium dioxide on the intermediate setting surface of two pieces of ultraviolet lamp plates
The corrugated plating of catalyst, the aerobic reaction section refer to that the biologic packing material that suspension is provided in this section of reaction tube, the biology are filled out
Material area load has aerobic microbiological, and one that the reaction tube is connect with second raft is arranged in the electronic rotating vane
End；
The electrocatalytic oxidation pole plate is connect with first battery, and the electronic rotating vane is connect with second battery,
The ultraviolet lamp plate is connect with first battery or second battery.
2. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the electrocatalytic oxidation pole plate
Anode is coating titanium anode, graphite electrode or lead base manganese alloy electrode.
3. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the electrocatalytic oxidation pole plate
Cathode uses metal material.
4. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the electrocatalytic oxidation pole plate
Electrode spacing is 40 centimetres.
5. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the electrocatalytic oxidation pole plate
Pressure is 3~10V DC voltage between electrode.
6. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the length of the aerobic reaction section
It is the 1/4~1/3 of the tube length of reaction tube.
7. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the diameter of the tubule is described
The 1/10~1/20 of the caliber of reaction tube.
8. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that the revolving speed of the electronic rotating vane is
50~300r/min.
9. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that on the inner wall of the reaction tube
It is provided with constent temperature heater.
10. pollution of river object Integrated Processing Unit as described in claim 1, which is characterized in that in the lower part of the reaction tube
It is connected with downward pendant hypostasis.
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