CN110028184A - A kind of method and apparatus with nanometer microwave ion induction technology processing sewage - Google Patents
A kind of method and apparatus with nanometer microwave ion induction technology processing sewage Download PDFInfo
- Publication number
- CN110028184A CN110028184A CN201910340731.3A CN201910340731A CN110028184A CN 110028184 A CN110028184 A CN 110028184A CN 201910340731 A CN201910340731 A CN 201910340731A CN 110028184 A CN110028184 A CN 110028184A
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- CN
- China
- Prior art keywords
- degradation
- sewage
- degradation treatment
- valve
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/302—Treatment of water, waste water, or sewage by irradiation with microwaves
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- 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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- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Inorganic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses a kind of equipment with nanometer microwave ion induction technology processing sewage, including aeration tank, aeration bottom of pond portion is provided with aeration plate, water outlet is arranged in the top of aeration tank, water outlet is connected with degradation treatment pipe, several threaded holes are fixed on degradation treatment pipe, degradation treatment tank is threaded on each threaded hole, degradation treatment tank surface is provided with strainer, container is plugged in degradation treatment tank, the outside of container is uniformly fixed with several the first degradation chambers, the center of container is fixed with the second degradation chamber, the both ends of each threaded hole are provided with the first shut-off valve, the both ends of each threaded hole are connected with shunt valve, the second shut-off valve is provided on shunt valve, degradation treatment pot bottom is provided with microwave source and ion source, the end of degradation treatment pipe is connected by return pipe with aeration tank.The present invention can improve the deficiencies in the prior art, improve the Homes Using TV of sewage disposal device.
Description
Technical field
The present invention relates to environmental technology field, especially a kind of method with nanometer microwave ion induction technology processing sewage
And equipment.
Background technique
With the development of China's industrialization and urbanization, the yield cumulative year after year of sewage.In order to protect environment, sewage needs
It could be discharged after purified treatment.In the prior art, it can effectively improve the catalytic effect of catalyst by using microwave, with
Improve sewage treating efficiency.But in more catalyst changeout every time, shutdown operation is needed, causes equipment operation rate not high.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of methods with nanometer microwave ion induction technology processing sewage
And equipment, the deficiencies in the prior art are able to solve, the Homes Using TV of sewage disposal device is improved.
In order to solve the above technical problems, the technical solution used in the present invention is as follows.
A kind of equipment with nanometer microwave ion induction technology processing sewage, including aeration tank, aeration bottom of pond portion are provided with
The inlet end of aeration plate, the aeration plate is connected separately with air intake duct and ozone air inlet pipe by triple valve, aeration tank
Water inlet is arranged in bottom, and water outlet is arranged in the top of aeration tank, and water outlet is connected with degradation treatment pipe, fixes on degradation treatment pipe
There are several threaded holes, degradation treatment tank is threaded on each threaded hole, degradation treatment tank surface is provided with strainer, degradation
Container is plugged in process tank, the outside of container is uniformly fixed with several the first degradation chambers, and the center of container is solid
Surely there is the second degradation chamber, active carbon and titanium dioxide are filled in the first degradation chamber, is plugged with iron in the second degradation chamber
First through hole, the both ends of each threaded hole are respectively arranged at the top and bottom of stick, the first degradation chamber and the second degradation chamber
It is provided with the first shut-off valve, the both ends of each threaded hole are connected with shunt valve, and the second shut-off valve is provided on shunt valve, degrade
Processing pot bottom is provided with microwave source and ion source, and the end of degradation treatment pipe is connected by return pipe with aeration tank.
Preferably, being fixed with web plate in the first degradation chamber, titanium dioxide is located at the lower section of web plate, active carbon position
In the top of web plate.
Preferably, being connected between the first degradation chamber and the second degradation chamber by the second through-hole.
Preferably, the web plate surface is provided with oven wire mesh blanket.
Preferably, being fixed with shield outside the threaded hole, handle hole is offered on shield.
A kind of processing method of the above-mentioned equipment with nanometer microwave ion induction technology processing sewage, including following step
It is rapid:
A, treatment sewage is injected into aeration tank, the ratio between injection rate of air and ozone is controlled in 5:1, starts to carry out at aeration
Reason；
B, enter degradation treatment pipe from water outlet by the sewage that aeration tank is handled, catalytic degradation, part are carried out in container
The sewage of processing passes back into aeration tank by return pipe；The ratio between loading of active carbon and titanium dioxide is 2:1, the function of microwave source
Rate is 550W, and the power of ion source is 120W；
C, when the catalyst in container needs replacing, the first shut-off valve is closed, corresponding second shut-off valve is opened, will degrade
Process tank screws out the replacement for carrying out catalyst.
Brought beneficial effect is by adopting the above technical scheme: the present invention is several by the way that catalytic degradation equipment to be divided into
A series unit realizes the independent operating of each unit, replacement convenient for safeguarding.When needing to be serviced, pass through shunt valve pair
It is isolated to maintenance unit, then screwing out degradation treatment tank can be operated, convenient and efficient.By using active carbon, two
Titanium oxide and iron can efficiently use microwave and ion energy as united catalyst, microwave and ion conduct joint catalytic way
Amount improves catalytic decomposition efficiency.Ozone is added in aeration tank, oxidation sterilizing and decomposition can be not only carried out to sewage, but also
When being contacted with iron staff, ferric ion can be decomposited, and then flocculation sedimentation is carried out to sewage, improve treatment effect.By setting
Flow tube is put back into, a small amount of ferric ion is imported in aeration tank, the service life of filtrate can be effectively extended.Titanium dioxide is placed on
Close to the position of microwave source and ion source, its characteristic high to microwave and Ions Absorption rate can use, improve entire first drop
The operating temperature for solving chamber, to improve catalytic rate.Ferric ion can diffuse into the first degradation chamber by the second through-hole,
Reduce pollution of the granule foreign in sewage to catalyst.By the way that oven wire mesh blanket is arranged, can effective adsorption precipitation object, thus
Guarantee effective contact area of catalyst and sewage.
Detailed description of the invention
Fig. 1 is the structure chart of a specific embodiment of the invention.
Fig. 2 is the structure chart of degradation treatment tank in a specific embodiment of the invention.
In figure: 1, aeration tank；2, aeration plate；3, triple valve；4, air intake duct；5, ozone air inlet pipe；6, water inlet；7,
Water outlet；8, degradation treatment pipe；9, threaded hole；10, degradation treatment tank；11, strainer；12, oven wire mesh blanket；13, container；
14, the first degradation chamber；15, the second degradation chamber；16, the first shut-off valve；17, shunt valve；18, the second shut-off valve；19, first
Through-hole；20, microwave source；21, web plate；22, return pipe；23, the second through-hole；24, shield；25, handle hole；26, ion source.
Specific embodiment
The standardized element used in the present invention can commercially, and shaped piece is according to specification and attached drawing
Record can carry out customized, and the specific connection type of each part is all made of in the prior art mature bolt, rivet, weldering
The conventional means such as connect, paste, this will not be detailed here.
Referring to Fig.1-2, a specific embodiment of the invention includes aeration tank 1, and 1 bottom of aeration tank is provided with aeration plate 2,
The inlet end of the aeration plate 2 is connected separately with air intake duct 4 and ozone air inlet pipe 5, the bottom of aeration tank 1 by triple valve 3
Portion is arranged water inlet 6, and the top of aeration tank 1 is arranged water outlet 7, and water outlet 7 is connected with degradation treatment pipe 8, on degradation treatment pipe 8
Several threaded holes 9 are fixed with, degradation treatment tank 10, the setting of 10 surface of degradation treatment tank are threaded on each threaded hole 9
There is strainer 11, container 13 is plugged in degradation treatment tank 10, the outside of container 13 is uniformly fixed with several the first degradations
Chamber 14, the center of container 13 are fixed with the second degradation chamber 15, are filled with active carbon and dioxy in the first degradation chamber 14
Change titanium, iron staff, the top and bottom point of the first degradation chamber 14 and the second degradation chamber 15 are plugged in the second degradation chamber 15
It is not provided with first through hole 19, the both ends of each threaded hole 9 are provided with the first shut-off valve 16, the both ends connection of each threaded hole 9
There is shunt valve 17, the second shut-off valve 18 is provided on shunt valve 17,10 bottom of degradation treatment tank is provided with microwave source 20 and ion
Source 26, microwave source 20 are light wave generator, and ion source 26 is electron beam emitter, and the end of degradation treatment pipe 8 passes through return pipe
22 are connected with aeration tank 1.It is fixed with web plate 21 in first degradation chamber 14, titanium dioxide is located at the lower section of web plate 21, active carbon
Positioned at the top of web plate 21.It is connected between first degradation chamber 14 and the second degradation chamber 15 by the second through-hole 23.Web plate
21 surfaces are provided with oven wire mesh blanket 12.It is fixed with shield 24 outside threaded hole 9, handle hole 25 is offered on shield 24.
A kind of processing method of the above-mentioned equipment with nanometer microwave ion induction technology processing sewage, including following step
It is rapid:
A, treatment sewage is injected into aeration tank 1, the ratio between injection rate of air and ozone is controlled in 5:1, starts to be aerated
Processing；
B, enter degradation treatment pipe 8 from water outlet 7 by the sewage that aeration tank 1 is handled, catalytic degradation carried out in container 13,
The sewage of part processing passes back into aeration tank 1 by return pipe 22, and reflux ratio is 10%；The filling of active carbon and titanium dioxide
The ratio between amount is 2:1, and the power of microwave source 20 is 550W, and the power of ion source is 120W；
C, when the catalyst in container 13 needs replacing, the first shut-off valve 16 is closed, opens corresponding second shut-off valve 18,
Degradation treatment tank 10 is screwed out to the replacement for carrying out catalyst.
In the description of the present invention, it is to be understood that, term " longitudinal direction ", " transverse direction ", "upper", "lower", "front", "rear",
The orientation or positional relationship of the instructions such as "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is based on attached drawing institute
The orientation or positional relationship shown is merely for convenience of the description present invention, rather than the device or element of indication or suggestion meaning must
There must be specific orientation, be constructed and operated in a specific orientation, therefore be not considered as limiting the invention.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (6)
1. a kind of equipment with nanometer microwave ion induction technology processing sewage, including aeration tank (1), aeration tank (1) bottom are set
It is equipped with aeration plate (2), it is characterised in that: the inlet end of the aeration plate (2) is connected separately with air inlet by triple valve (3)
(4) and ozone air inlet pipe (5) are managed, water inlet (6) are arranged in the bottom of aeration tank (1), and water outlet is arranged in the top of aeration tank (1)
(7), water outlet (7) is connected with degradation treatment pipe (8), several threaded holes (9), each spiral shell are fixed on degradation treatment pipe (8)
It is threaded on pit (9) degradation treatment tank (10), degradation treatment tank (10) surface is provided with strainer (11), degradation treatment tank
(10) it is plugged with container (13) in, the outside of container (13) is uniformly fixed with several the first degradations chamber (14), accommodates
The center of device (13) is fixed with the second degradation chamber (15), is filled with active carbon and titanium dioxide in the first degradation chamber (14),
Iron staff, the top and bottom point of the first degradation chamber (14) and the second degradation chamber (15) are plugged in second degradation chamber (15)
It is not provided with first through hole (19), the both ends of each threaded hole (9) are provided with the first shut-off valve (16), each threaded hole (9)
Both ends are connected with shunt valve (17), are provided on shunt valve (17) the second shut-off valve (18), the setting of degradation treatment tank (10) bottom
There are microwave source (20) and ion source (26), the end of degradation treatment pipe (8) is connected by return pipe (22) with aeration tank (1).
2. the equipment according to claim 1 with nanometer microwave ion induction technology processing sewage, it is characterised in that: described
It is fixed with web plate (21) in first degradation chamber (14), titanium dioxide is located at the lower section of web plate (21), and active carbon is located at web plate
(21) top.
3. the equipment according to claim 2 with nanometer microwave ion induction technology processing sewage, it is characterised in that: described
It is connected between first degradation chamber (14) and the second degradation chamber (15) by the second through-hole (23).
4. the equipment according to claim 3 with nanometer microwave ion induction technology processing sewage, it is characterised in that: described
Web plate (21) surface is provided with oven wire mesh blanket (12).
5. the equipment according to claim 1 with nanometer microwave ion induction technology processing sewage, it is characterised in that: described
It is fixed with shield (24) outside threaded hole (9), handle hole (25) is offered on shield (24).
6. with the processing of the equipment of nanometer microwave ion induction technology processing sewage described in a kind of claim 1-5 any one
Method, it is characterised in that the following steps are included:
A, treatment sewage is injected into aeration tank (1), the ratio between injection rate of air and ozone is controlled in 5:1, starts to be exposed
Gas disposal；
B, the sewage by aeration tank (1) processing enters degradation treatment pipe (8) from water outlet (7), carries out in container (13)
The sewage of catalytic degradation, part processing passes back into aeration tank (1) by return pipe (22)；The loading of active carbon and titanium dioxide
The ratio between be 2:1, the power of microwave source (20) is 550W, and the power of ion source is 120W；
C, it when the catalyst in container (13) needs replacing, closes the first shut-off valve (16), opens corresponding second cut-off
Degradation treatment tank (10) are screwed out the replacement for carrying out catalyst by valve (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910340731.3A CN110028184B (en) | 2019-04-25 | 2019-04-25 | Method and equipment for treating sewage by using nano microwave ion induction technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910340731.3A CN110028184B (en) | 2019-04-25 | 2019-04-25 | Method and equipment for treating sewage by using nano microwave ion induction technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110028184A true CN110028184A (en) | 2019-07-19 |
| CN110028184B CN110028184B (en) | 2021-07-06 |
Family
ID=67240375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910340731.3A Active CN110028184B (en) | 2019-04-25 | 2019-04-25 | Method and equipment for treating sewage by using nano microwave ion induction technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110028184B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111849566A (en) * | 2020-07-30 | 2020-10-30 | 中国科学院过程工程研究所 | Blast furnace gas hydrolysis desulfurization device and method |
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-
2019
- 2019-04-25 CN CN201910340731.3A patent/CN110028184B/en active Active
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| CN1544360A (en) * | 2003-11-13 | 2004-11-10 | 哈尔滨工业大学 | Multi-phase concentration, microwave synergy, catalytic oxidation method for degrading organic pollutant in water |
| CN1785830A (en) * | 2005-10-27 | 2006-06-14 | 武汉科技学院 | Microwave plasma fortified internal electrolysis photocatelysis oxidation integrated water treatment equipment |
| US20130023448A1 (en) * | 2011-07-18 | 2013-01-24 | A3Environ Technologies Llc | Methods for Treating Hydrocarbon-Servicing Fluids and Wastewater and Fluids Produced Using the Same |
| CN102380316A (en) * | 2011-09-22 | 2012-03-21 | 张慧春 | Horizontal pressure leaching composite membrane filtering system |
| CN103159354A (en) * | 2013-03-06 | 2013-06-19 | 宁波大学 | Microwave coupling photochemical catalysis wastewater degradation reactor for fine entrapment of nanometer catalyst |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111849566A (en) * | 2020-07-30 | 2020-10-30 | 中国科学院过程工程研究所 | Blast furnace gas hydrolysis desulfurization device and method |
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| Publication number | Publication date |
|---|---|
| CN110028184B (en) | 2021-07-06 |
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