CN205773582U - A kind of sewage-treatment plant based on ozone catalytic technology - Google Patents
A kind of sewage-treatment plant based on ozone catalytic technology Download PDFInfo
- Publication number
- CN205773582U CN205773582U CN201620752391.7U CN201620752391U CN205773582U CN 205773582 U CN205773582 U CN 205773582U CN 201620752391 U CN201620752391 U CN 201620752391U CN 205773582 U CN205773582 U CN 205773582U
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- China
- Prior art keywords
- filter course
- water tank
- dividing plate
- sewage
- water
- 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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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000010865 sewage Substances 0.000 title claims abstract description 31
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 15
- 238000005516 engineering process Methods 0.000 title claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 230000008676 import Effects 0.000 claims abstract description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 7
- 239000012528 membrane Substances 0.000 claims description 6
- 230000000903 blocking effect Effects 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 238000009423 ventilation Methods 0.000 claims 3
- 238000005202 decontamination Methods 0.000 abstract description 4
- 230000003588 decontaminative effect Effects 0.000 abstract description 4
- 230000003647 oxidation Effects 0.000 description 9
- 238000007254 oxidation reaction Methods 0.000 description 9
- 230000008859 change Effects 0.000 description 6
- 230000001954 sterilising effect Effects 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 244000144992 flock Species 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000010405 reoxidation reaction Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000009428 plumbing Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of sewage-treatment plant based on ozone catalytic technology, relate to sewage treatment area, including water tank, water tank is provided with water inlet and outlet, under upper, the first filter course it is sequentially provided with in water tank, dividing plate and the second filter course, if being wherein provided with dried layer drainage screen in the first filter course, water tank is externally provided with ozonator, ozonator is provided with the breather being passed through water tank, dividing plate is provided with electromagnetic valve, the lower surface of dividing plate is provided with pressure transducer, pressure transducer is connected with electromagnetic valve, it is provided with activated carbon in second filter course, the lower section of the second filter course is provided with bypass outlet, backflow import it is provided with between first filter course and dividing plate, it is provided with return duct between backflow import and bypass outlet, backflow import is provided with water pump and is connected.This device utilizes ozone to carry out sewage disposal, and the water in water tank is carried out aoxidizing decontamination by the ozone that this device utilizes ozonator to produce.
Description
Technical field
This utility model relates to sewage treatment area, is specifically related to a kind of sewage disposal based on ozone catalytic technology dress
Put.
Background technology
Ozone has extremely strong oxidability, therefore has extremely strong bactericidal action, decolouring, deodorize, de-taste effect and divides
Solution effect.
Sterilization can be used for: upper and lower water, swimming-pool water, the sterilizing of drinking water etc.;Food storage indoor sterilizing:
The air cleanings such as hospital, school, kindergarten, office, food processing factory, pharmaceutical factory;Utensil class sterilizing, hospital sewage,
Sterilizing of sanitary sewage etc..
Decolouring, deodorize, de-taste effect can be used for: decolorizing printing and dyeing waste water, night soil-treatment, the decolouring taste removal of plumbing, cultivation
Field deodorization etc., the purification deodorize of sewer.
Oxidation: the oxidation of inorganic matter, Chen Tie, manganese in water, the process of cyanide wastewater, ore treatment etc..Oxidation operation divides
Solve, municipal administration, Industrial Wastewater Treatment, micro-polluted water treatment, COD elimination etc., surface activation, surface properties (carbon blacksurface attribute,
Fiber surface attribute, frosting attribute), the synthesis of spice, change structure etc..Combustion in IC engine agent, rocket oxidizer etc..
Ozone has the strongest oxidizing force, is currently known one of the strongest oxidant.Ozone use in sewage disposal
Way is widest, and its principle is all the strong oxidizing property of the ozone utilized.After ozone decomposed, it is decomposed into oxygen.
Utility model content
For the deficiencies in the prior art, the purpose of this utility model be to provide a kind of multiple times of filtration based on ozone catalytic
The sewage-treatment plant of technology.
This utility model solves the technical problem that and can realize by the following technical solutions: a kind of based on ozone catalytic skill
The sewage-treatment plant of art, including water tank, the top of water tank is provided with the lower end of water inlet and water tank and is provided with outlet, in outlet
It is provided with blocking, in wherein said water tank, under upper, is sequentially provided with the first filter course, dividing plate and the second filter course, wherein the first mistake
If being provided with dried layer drainage screen in filtering layer, drainage screen mesh under upper is sequentially reduced, and water tank is externally provided with ozonator, and ozone is sent out
Raw device is provided with breather, and water tank is being provided with passage between the first filter course and dividing plate at dividing plate, the end of breather
End connection is in passage, and dividing plate is provided with electromagnetic valve, and the lower surface of dividing plate is provided with pressure transducer, pressure transducer and electromagnetism
Valve is connected, and is provided with activated carbon in the second filter course, and the lower section of the second filter course is provided with bypass outlet, the first filter course and dividing plate it
Between be provided with backflow import, be provided with between backflow import and bypass outlet can flow tube, backflow import is provided with water pump and is connected, described in go out
The mouth of a river is positioned at the lower section of bypass outlet.
Preferably, described water tank is provided with opening at the second filter course, and opening is provided with hinged cover plate, sets below water tank
Having reserving liquid tank, reserving liquid tank to be provided with pod apertures, pod apertures is provided with mozzle, and described bypass outlet is provided with three-way valve, water conservancy diversion
Pipe can flow tube be both connected on three-way valve with described.
Preferably, described passage be arranged over observation port, observation port is provided with transparent access panel.
Preferably, described outlet is provided with semipermeable membrane.
Preferably, described breather is provided with check valve.
Preferably, described passage, backflow import, bypass outlet, pod apertures are equipped with sealing gasket.
Provide the benefit that: this device utilizes ozone to carry out sewage disposal, and this device utilizes ozonator to produce
Water in water tank is carried out aoxidizing decontamination by ozone.The first filter course in the water tank of this device can filter oarse-grained dirt,
First filter course is made up of some drainage screens, can filter successively, improves the efficiency filtered.Moisture can be separated by dividing plate, makes
Obtaining ozone can be by sewage oxidation, it is ensured that sewage cannot flow under dividing plate before not aoxidizing.Dividing plate can be according to pressure sensing
The water yield on device, i.e. dividing plate, and open and close electromagnetic valve, the water after oxidation can be carried out secondary filter by the second filter course, removes water
Flocks after middle oxidation.In addition the water after the second filter course filters can be back to above dividing plate by return duct, reoxidation,
And improve purifying rate.Additionally, opening and cover plate make the second filter course to change, reserving liquid tank makes the second filter course change
Time, the water under dividing plate can flow in reserving liquid tank, it is to avoid the unnecessary water yield runs off.Semipermeable membrane on outlet can be carried out
After filtration once, it is ensured that obtain is all pure water.Check valve on air-vent water of can weaving is back in ozonator,
And damage ozonator.Transparent access panel can observe the water yield on dividing plate, it is ensured that ozone is passed through in sewage, it is to avoid ozone
Leakage.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of sewage-treatment plant based on ozone catalytic technology of this utility model;
Wherein 1, water tank;2, water inlet;3, outlet;4, blocking;5, ozonator;6, the first filter course;7, dividing plate;
8, the second filter course;9, drainage screen;10, passage;11, breather;12, check valve;13, observation port;14, access panel;15, pressure
Force transducer;16, electromagnetic valve;17, reflux import;18, bypass outlet;19, return duct;20, water pump;21, opening;22, cover plate;
23, reserving liquid tank;24, pod apertures;25, mozzle;26, three-way valve;27, semipermeable membrane.
Detailed description of the invention
Describe preferred implementation of the present utility model below in conjunction with the accompanying drawings in detail.
Fig. 1 shows the detailed description of the invention of a kind of sewage-treatment plant based on ozone catalytic technology of this utility model: one
Kind of sewage-treatment plant based on ozone catalytic technology, including water tank 1, the top of water tank 1 is provided with water inlet 2 and water tank 1 time
End is provided with outlet 3, is provided with blocking 4 in outlet 3, be sequentially provided with under upper in wherein said water tank 1 first filter course 6,
Dividing plate 7 and the second filter course 8, if being wherein provided with dried layer drainage screen 9 in the first filter course 6, mesh is successively under upper for drainage screen 9
Reducing, water tank 1 is externally provided with ozonator 5, and ozonator 5 is provided with breather 11, water tank 1 the first filter course 6 with every
Being provided with passage 10 at dividing plate 7 between plate 7, the end of breather 11 connects in passage 10, and dividing plate 7 is provided with electricity
Magnet valve 16, the lower surface of dividing plate 7 is provided with pressure transducer 15, and pressure transducer 15 is connected with electromagnetic valve 16, in the second filter course 8
Being provided with activated carbon, the lower section of the second filter course 8 is provided with bypass outlet 18, is provided with backflow import between the first filter course 6 and dividing plate 7
17, it is provided with meeting flow tube between backflow import 17 and bypass outlet 18, backflow import 17 is provided with water pump 20 and is connected, described outlet
3 lower sections being positioned at bypass outlet 18.
It should be noted that described water tank 1 is provided with opening 21 at the second filter course 8, opening 21 is provided with hinged lid
Plate 22, is provided with reserving liquid tank 23 below water tank 1, reserving liquid tank 23 is provided with pod apertures 24, and pod apertures 24 is provided with mozzle 25, described
Bypass outlet 18 is provided with three-way valve 26, and mozzle 25 can flow tube be both connected on three-way valve 26 with described.
Described passage 10 be arranged over observation port 13, observation port 13 is provided with outlet described in transparent access panel 14
3 are provided with semipermeable membrane 27.Described breather 11 is provided with check valve 12.Described passage 10, backflow import 17, bypass outlet
18, it is equipped with sealing gasket in pod apertures 24.
Being passed through water tank 1 from water inlet 2 by sewage, sewage filters from the first filter course 6, and the water after filtration retains
On dividing plate 7.When observing water on access panel 14, ozonator 5 is passed through ozone, carries out aoxidizing decontamination.When pressure passes
When sensor 15 detects the hypervolia on dividing plate 7, electromagnetic valve 16 is opened so that water flows to dividing plate 7 times, at the second filter course 8
Carry out second time to filter.Water can be flowed back on dividing plate 7 by water pump 20 by return duct 19 again afterwards, then carries out oxidation filtration, only
Water after change can be flowed out by outlet 3.
When dirt is too much on the first filter course 6, the first filter course 6 can be taken out at water inlet 2 replacing.When second
When filter course 8 dirt is too much, electromagnetic valve 16, regulating three-way valve 26 can be closed so that 7 times most water of dividing plate flow to liquid storage
In case 23, it is ensured that there is no water at opening 21, open opening 21, the second filter course 8 is taken out replacing.After closing upper shed 21, regulation
Three-way valve 26, opens water pump 20 so that the water in reserving liquid tank 23 returns to, on dividing plate 7, work as storage by mozzle 25 and return duct 19
After in liquid case 23, the water yield evacuates, regulating three-way valve 26 makes bypass outlet 18 communicate with backflow import 17.
Based on above-mentioned, this device utilizes ozone to carry out sewage disposal, and it is smelly that this device utilizes that ozonator 5 produces
Water in water tank 1 is carried out aoxidizing decontamination by oxygen.The first filter course 6 in the water tank 1 of this device can filter oarse-grained dirt,
First filter course 6 is made up of some drainage screens 9, can filter successively, improves the efficiency filtered.Moisture can be separated by dividing plate 7,
Make the ozone can be by sewage oxidation, it is ensured that sewage cannot flow into dividing plate 7 times before not aoxidizing.Dividing plate 7 can be according to pressure
The water yield on sensor 15, i.e. dividing plate 7, and open and close electromagnetic valve 16, the water after oxidation can be carried out secondary mistake by the second filter course 8
Filter, removes the flocks after water oxygen.In addition the water after the second filter course 8 filters can be back to dividing plate 7 by return duct 19
Top, reoxidation, and improve purifying rate.Additionally, opening 21 and cover plate 22 make the second filter course 8 to change, reserving liquid tank
23 when making the second filter course 8 change, and the water under dividing plate 7 can flow in reserving liquid tank 23, it is to avoid the unnecessary water yield runs off.Go out
Semipermeable membrane 27 on the mouth of a river 3 can carry out last filtration, it is ensured that obtain is all pure water.Check valve 12 on air-vent
Water of can weaving is back in ozonator 5, and damages ozonator 5.Transparent access panel 14 can be observed on dividing plate 7
The water yield, it is ensured that ozone is passed through in sewage, it is to avoid the leakage of ozone.
The foregoing is only embodiment of the present utility model, not thereby limit the scope of the claims of the present utility model, every
Utilize equivalent structure or equivalence flow process conversion that this utility model description and accompanying drawing content made, or be directly or indirectly used in
Other relevant technical fields, are the most in like manner included in scope of patent protection of the present utility model.
Claims (6)
1. a sewage-treatment plant based on ozone catalytic technology, including water tank, the top of water tank is provided with water inlet and water tank
Lower end be provided with outlet, be provided with blocking in outlet, it is characterised in that: under upper, is sequentially provided with the first mistake in described water tank
Filtering layer, dividing plate and the second filter course, if being wherein provided with dried layer drainage screen in the first filter course, mesh is successively under upper for drainage screen
Reduce, water tank is externally provided with ozonator, and ozonator is provided with breather, water tank between the first filter course and dividing plate
Being provided with passage at dividing plate, the end of breather connects in passage, and dividing plate is provided with electromagnetic valve, the lower surface of dividing plate
Being provided with pressure transducer, pressure transducer is connected with electromagnetic valve, is provided with activated carbon in the second filter course, the lower section of the second filter course
It is provided with bypass outlet, is provided with backflow import between the first filter course and dividing plate, between backflow import and bypass outlet, is provided with backflow
Pipe, backflow import is provided with water pump and is connected, and described outlet is positioned at the lower section of bypass outlet.
A kind of sewage-treatment plant based on ozone catalytic technology, it is characterised in that: described water tank
Being provided with opening at the second filter course, opening is provided with hinged cover plate, is provided with reserving liquid tank below water tank, and reserving liquid tank is provided with leads
Discharge orifice, pod apertures is provided with mozzle, and described bypass outlet is provided with three-way valve, and mozzle and described return duct are both connected to three
On logical valve.
A kind of sewage-treatment plant based on ozone catalytic technology, it is characterised in that: described ventilation
Hole be arranged over observation port, observation port is provided with transparent access panel.
A kind of sewage-treatment plant based on ozone catalytic technology, it is characterised in that: described water outlet
Mouth is provided with semipermeable membrane.
A kind of sewage-treatment plant based on ozone catalytic technology, it is characterised in that: described ventilation
Pipe is provided with check valve.
A kind of sewage-treatment plant based on ozone catalytic technology, it is characterised in that: described ventilation
It is equipped with sealing gasket in hole, backflow import, bypass outlet, pod apertures.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620752391.7U CN205773582U (en) | 2016-07-14 | 2016-07-14 | A kind of sewage-treatment plant based on ozone catalytic technology |
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CN201620752391.7U CN205773582U (en) | 2016-07-14 | 2016-07-14 | A kind of sewage-treatment plant based on ozone catalytic technology |
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CN205773582U true CN205773582U (en) | 2016-12-07 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265707A (en) * | 2017-08-21 | 2017-10-20 | 湖州练市成宇丝织厂 | A kind of processing unit of sewage foul smell |
CN108218041A (en) * | 2018-02-01 | 2018-06-29 | 广州粤禹环保科技有限公司 | A kind of medical clinic sewage disposal cleaning system and its control method |
-
2016
- 2016-07-14 CN CN201620752391.7U patent/CN205773582U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265707A (en) * | 2017-08-21 | 2017-10-20 | 湖州练市成宇丝织厂 | A kind of processing unit of sewage foul smell |
CN107265707B (en) * | 2017-08-21 | 2020-04-28 | 亚太泵阀有限公司 | Sewage odor treatment device |
CN108218041A (en) * | 2018-02-01 | 2018-06-29 | 广州粤禹环保科技有限公司 | A kind of medical clinic sewage disposal cleaning system and its control method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 |