CN108191150A - A kind of vehicle moving sewage treatment equipment - Google Patents
A kind of vehicle moving sewage treatment equipment Download PDFInfo
- Publication number
- CN108191150A CN108191150A CN201711483996.6A CN201711483996A CN108191150A CN 108191150 A CN108191150 A CN 108191150A CN 201711483996 A CN201711483996 A CN 201711483996A CN 108191150 A CN108191150 A CN 108191150A
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- pond
- waste water
- dosing pond
- dosing
- sewage treatment
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- 239000010865 sewage Substances 0.000 title claims abstract description 26
- 239000002351 wastewater Substances 0.000 claims abstract description 72
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 37
- 230000003647 oxidation Effects 0.000 claims abstract description 34
- 230000001112 coagulating effect Effects 0.000 claims abstract description 26
- 238000001556 precipitation Methods 0.000 claims abstract description 26
- 238000005660 chlorination reaction Methods 0.000 claims abstract description 15
- 239000003814 drug Substances 0.000 claims abstract description 12
- 239000010802 sludge Substances 0.000 claims abstract description 11
- 238000004062 sedimentation Methods 0.000 claims abstract description 10
- 239000006228 supernatant Substances 0.000 claims abstract description 10
- 238000005276 aerator Methods 0.000 claims abstract description 8
- 230000002572 peristaltic effect Effects 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 239000012528 membrane Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 241000894006 Bacteria Species 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 4
- 235000009161 Espostoa lanata Nutrition 0.000 claims description 3
- 240000001624 Espostoa lanata Species 0.000 claims description 3
- 206010067868 Skin mass Diseases 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 3
- 238000001471 micro-filtration Methods 0.000 claims description 3
- 231100000572 poisoning Toxicity 0.000 claims description 3
- 230000000607 poisoning effect Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- 238000005345 coagulation Methods 0.000 claims 1
- 230000015271 coagulation Effects 0.000 claims 1
- 239000000945 filler Substances 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 238000004659 sterilization and disinfection Methods 0.000 claims 1
- 229940079593 drug Drugs 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 238000005868 electrolysis reaction Methods 0.000 description 5
- 238000011953 bioanalysis Methods 0.000 description 4
- 238000005374 membrane filtration Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000006065 biodegradation reaction Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 206010013082 Discomfort Diseases 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000009303 advanced oxidation process reaction Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 244000045947 parasite Species 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003643 water by type Substances 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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- 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
- C02F1/30—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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46176—Galvanic cells
-
- 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
-
- 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
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle
-
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- 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
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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention provides a kind of vehicle moving sewage treatment equipment,Including babinet,Wheel is provided with below babinet,Pretreatment pool is equipped in babinet,Advanced oxidation pond,Coagulative precipitation tank,Biochemistry pool,Sludge concentration tank and battery limits,Pretreatment pool is divided into the first interconnected dosing pond from top to bottom,Second dosing pond and third dosing pond,Medicine machine is placed in battery limits,Peristaltic pump,Suction filter pump,Control panel,Aerator,Chlorination equipment and filter device,Waste water is drawn into the first dosing pond by peristaltic pump,Waste water flows into the second dosing pond and third dosing pond successively,Then advanced oxidation pond is flowed by the first aperture being arranged on third dosing pond,And the second orifice by being arranged on advanced oxidation pond flows into coagulative precipitation tank,It is settled in coagulative precipitation tank,The supernatant of waste water is flowed into biochemistry pool by the downflow weir being arranged on coagulative precipitation tank after sedimentation,Then filter device is drawn by suction filter pump and flows into chlorination equipment after filtering and be disinfected after discharge.
Description
Technical field
The present invention relates to wastewater treatment equipment more particularly to a kind of vehicle moving sewage treatment equipments.
Background technology
High-level oxidation technology is widely used in wastewater treatment in recent years, and high-level oxidation technology is in the difficult biology drop of processing
Solution has that equipment is small, easy to operate, COD (Chemical Oxygen Demand, chemical oxygen demand in terms of high concentrated organic wastewater
Amount) removal rate height, good decolorizing effect, the time is short, can improve the advantages such as biodegradability, and it is a kind of effective wastewater processing technology.
In high-level oxidation technology with iron-carbon micro-electrolysis and Fenton oxidation application it is more ripe, most widely used, but iron-carbon micro-electrolysis with
There are the shortcomings that high energy consumption for Fenton oxidation；Bioanalysis is at low cost, easy to operate, has preferable place to easily biological-degradable organic wastewater
Manage effect, but its to difficult for biological degradation and toxic wastewater treatment effect it is bad.Therefore, advanced oxidation processes are combined with bioanalysis is
A kind of waste water two stage treatment technique for having much prospect.Membrane filtration application is quite wide in tertiary treatment technology, but membrane pollution problem is urgently
To be solved, numerous studies, which show that membrane filtration is combined with bioanalysis, can alleviate fouling membrane.Therefore electrochemistry, bioanalysis and membrane filtration
Three acts synergistically, not only controllable costs, but also can efficiently and thoroughly handle high-leveled and difficult waste water.
At present, there are 3 main problems in the water process of environment-friendly engineering：(1) some factory's waters are unstable, sewage disposal
Batch interval time is long, sewage generation position is not fixed, water is small, concentration of wastewater is big, therefore these factory's discomforts build sewage jointly
Treatment plant；(2) building sewage treatment plant needs to occupy larger land area, and of high cost；(3) single materialization or it is biochemical
Through sewage drainage standard can not be met.
Invention content
In view of this, the present invention provides a kind of vehicle moving sewage treatment equipments compact-sized, floor space is small.
The present invention provides a kind of vehicle moving sewage treatment equipment, and including babinet, the lower section setting of the babinet is useful
Be equipped in the wheel of walking, in the babinet pretreatment pool, advanced oxidation pond, coagulative precipitation tank, biochemistry pool, sludge concentration tank and
Battery limits, the pretreatment tank are divided into the first dosing pond, the second dosing pond and third dosing pond, first dosing from top to bottom
Pond is connected with the second dosing pond, and the second dosing pond is connected with third dosing pond, and medicine machine, compacted is placed in the battery limits
Waste water is drawn into first and added by dynamic pump, suction filter pump, control panel, aerator, chlorination equipment and filter device, the peristaltic pump
In medicine pond, the waste water into the first dosing pond flows into the second dosing pond and third dosing pond successively, then by being arranged on third
The first aperture on dosing pond flows into advanced oxidation pond, into advanced oxidation pond waste water by being arranged on advanced oxidation pond
Second orifice flows into coagulative precipitation tank, is settled in coagulative precipitation tank, the supernatant of waste water is mixed by being arranged on after sedimentation
Downflow weir on solidifying sedimentation basin is flowed into biochemistry pool, completes to be drawn into filter device process by suction filter pump after reacting in biochemistry pool
It flows into chlorination equipment after filter to be disinfected after discharge, the control panel controls medicine machine to the first dosing pond, the second dosing pond
With dosing in third dosing pond, the aerator is supplied oxygen into biochemistry pool, the sludge concentration tank to collect pretreatment pool,
Sludge in coagulative precipitation tank and biochemistry pool.
Further, it is added in the first dosing pond and adjusts liquid to adjust the pH of waste water acid-base value, described second adds
Aluminium polychloride or demulsifier are added in medicine pond, adds to adsorb the poly- of the suspended particulate in waste water in the third dosing pond
Acrylamide is placed in the second dosing pond to remove the second tilted plate separator of the suspended particulate in waste water.
Further, biologic packing material and membrane module are placed in the biochemistry pool, the biologic packing material is carrying out waste water
Biodegradation, the membrane module is to the organic matter in filtered wastewater.
Further, the biologic packing material selects any one of fibre bundle, fibrous nodules, cotton ball or haydite, the film
Component is middle control tunica fibrosa or plate membrane, and the membrane component in the membrane module selects appointing in microfiltration membranes, ultrafiltration membrane or NF membrane
It is a kind of.
Further, hold to adsorb the polyacrylamide of the suspended particulate in waste water in the coagulative precipitation tank, and
It is placed with to remove the first tilted plate separator of the suspended particulate in waste water.
Further, the advanced oxidation pond is iron-carbon micro-electrolysis pond or Fenton oxidation electrolytic cell.
Further, the filter device is more medium filter or carbon filter.
Further, the chlorination equipment carries out poisoning bacterium of going out by ultraviolet light to water.
Further, the bottom in the first dosing pond is equipped with third aperture, by third aperture by the first dosing pond and
Second dosing pond connects, and the bottom in the second dosing pond is equipped with the 4th aperture, by the 4th aperture by the second dosing pond and the
Three dosing ponds connect.
Further, the pretreatment tank carries out waste water water quality adjustment and sedimentation obtains first order processing waste water, described
Generation oxidation reaction obtains second level processing waste water after first order processing waste water flows into advanced oxidation pond, and the second level processing is useless
Water flows into coagulative precipitation tank and realizes mud-water separation, obtains supernatant, and the supernatant carries out biodegradation after being flowed into biochemistry pool
And UF membrane, third level processing waste water is obtained, the third level processing waste water disappears further across the filtering of filter device, chlorination equipment
The water purification of discharge standard must be reached after poison.
The advantageous effect that technical solution provided by the invention is brought is：Sewage treatment equipment structure provided by the invention is tight
Gather, conveniently moving, floor space it is small, easy to operate, integration degree is higher；Equipment provided by the invention will be by that will pre-process
Pond, advanced oxidation pond, coagulative precipitation tank and biochemistry pool combine, and not only greatly improve water treatment effect, but also can have
Effect alleviates fouling membrane.
Description of the drawings
Fig. 1 is a kind of structure diagram of vehicle moving sewage treatment equipment of the present invention.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with attached drawing to embodiment party of the present invention
Formula is further described.
It please refers to Fig.1, the embodiment provides a kind of vehicle moving sewage treatment equipment, including babinet 1, case
The lower section of body 1 is provided with the wheel 11 for walking, and pretreatment pool 12, advanced oxidation pond 13, coagulative precipitation tank are equipped in babinet 1
14th, biochemistry pool 15, sludge concentration tank 16 and battery limits 17, pretreatment pool 12 are divided into the first dosing pond 121, second and add from top to bottom
Medicine pond 122 and third dosing pond 123, the bottom in the first dosing pond 121 are equipped with third aperture (not shown), pass through third aperture
First dosing pond 121 is connected with the second dosing pond 122, the bottom in the second dosing pond 122 is equipped with the 4th aperture, small by the 4th
Hole connects in the second dosing pond 122 with third dosing pond 123, and medicine machine 171 is placed in battery limits 17, peristaltic pump 172, is filtered
Pump 173, control panel 174, aerator 175, chlorination equipment 176 and filter device 177, waste water are drawn into through peristaltic pump 172
In first dosing pond 121, the waste water into the first dosing pond 121 flows into the second dosing pond 122 and third dosing pond 123 successively,
Then advanced oxidation pond 13 is flowed by the first aperture being arranged on third dosing pond 123, into the useless of advanced oxidation pond 13
Water flows into coagulative precipitation tank 14 by the second orifice being arranged on advanced oxidation pond 13, and it is heavy to occur in coagulative precipitation tank 14
Drop, the top of coagulative precipitation tank 14 is the supernatant of waste water after sedimentation, and the lower section of coagulative precipitation tank 14 is sludge, the supernatant of waste water
Liquid is flowed into biochemistry pool 15 by the downflow weir being arranged on coagulative precipitation tank 14, passes through pumping after completing reaction in biochemistry pool 15
Filter pump 173, which is drawn into filter device 177 and flows into chlorination equipment 176 after filtering, to be disinfected after discharge.
Sludge concentration tank 16 is collecting the sludge in pretreatment pool 12, coagulative precipitation tank 14 and biochemistry pool 15, biochemistry pool
Biologic packing material 151 and membrane module 152 are placed in 15, biologic packing material 151 is selected in fibre bundle, fibrous nodules, cotton ball or haydite
Any, membrane module 152 is middle control tunica fibrosa or plate membrane, and the membrane component in membrane module 152 is microfiltration membranes, ultrafiltration membrane or nanofiltration
Film, biologic packing material 151 is biodegradable to be carried out to waste water, and membrane module 152 is to the organic matter in filtered wastewater.
In one embodiment, added in the first dosing pond 121 and adjust liquid, the second dosing pond to adjust the pH of waste water acid-base value
Addition aluminium polychloride or demulsifier in 122, and place the second tilted plate separator to remove the suspended particulate in waste water
1221, addition is to adsorb the polyacrylamide of the suspended particulate in waste water in third dosing pond 123, the first dosing pond 121, the
Dosing substance in two dosing ponds 122 and third dosing pond 123 can be selected according to the water quality situation of waste water, when needing to locate
When the waste water of reason is oily waste water, 122 planted agent of the second dosing pond adds demulsifier.
Control panel 174 is connect with aerator 175, medicine machine 171, control panel 174 control aerator 175 to
It is supplied oxygen in biochemistry pool 15, control panel 174 controls medicine machine 171 to the first dosing pond 121, the second dosing pond 122 and third
123 dosing of dosing pond is effectively improved the working efficiency of wastewater treatment.
It holds to adsorb the polyacrylamide of the suspended particulate in waste water in coagulative precipitation tank 14, and is placed with
It, can using the first tilted plate separator and the second tilted plate separator 1221 except the first tilted plate separator of the suspended particulate in waste water
Granule foreign, suspension colloid, algae and the microorganism in waste water are removed well, also can remove stink and part iron, manganese.
Advanced oxidation pond 13 be iron-carbon micro-electrolysis pond or Fenton oxidation electrolytic cell, the COD in the waste water of processing
When higher, in order to reduce cost, iron-carbon micro-electrolysis pond and Fenton oxidation electrolytic cell can be combined as advanced oxidation pond 13, given up
Oxidation reaction occurs in advanced oxidation pond 13 for water to remove the persistent organic pollutants in waste water.
Filter device 177 selects more medium filter or carbon filter, can using more medium filter or carbon filter
The suspended matter in waste water is effectively removed, reduces mechanical damage and pollution of the water to reverse-osmosis membrane element.
Chlorination equipment 176 to water go out poisoning bacterium by ultraviolet light, by chlorination equipment 176 can will in water it is various thin
Bacterium, virus, parasite, algae and other pathogens are directly killed, and further improve the degree of purification of water.
In one embodiment, using the present invention vehicle moving sewage treatment equipment processing plant discharge waste water when, in advance
Processing pond 12 first carries out waste water water quality adjustment and sedimentation obtains first order processing waste water, and first order processing waste water flows into advanced
Oxidation reaction occurs after oxidation pond 13, most of organic matter that the first order handles in waste water is degraded and the first order handles waste water
Biodegradability is enhanced, and obtains second level processing waste water, and second level processing waste water flows into coagulative precipitation tank 14 and realizes mud-water separation,
Supernatant is obtained, supernatant carries out biodegradable and UF membrane after being flowed into biochemistry pool 15, obtains third level processing waste water, third
The water purification of discharge standard must be reached after grade processing waste water is filtered further across filter device 177, chlorination equipment 176 sterilizes.
Sewage treatment equipment provided by the invention is compact-sized, conveniently moving, floor space are small, easy to operate, integrated
Degree is higher；Equipment provided by the invention is by by pretreatment pool 12, advanced oxidation pond 13, coagulative precipitation tank 14 and biochemistry pool 15
With reference to not only greatly improving water treatment effect, but also can effectively alleviate fouling membrane.
Herein, the involved nouns of locality such as forward and backward, upper and lower are to be located in figure with parts in attached drawing and zero
Part mutual position defines, only for the purpose of expressing the technical solution clearly and conveniently.It should be appreciated that the noun of locality
Use should not limit the claimed range of the application.
In the absence of conflict, the feature in embodiment and embodiment herein-above set forth can be combined with each other.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all the present invention spirit and
Within principle, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention.
Claims (10)
1. a kind of vehicle moving sewage treatment equipment, which is characterized in that including babinet, be provided with and be used for below the babinet
The wheel of walking, the babinet is interior to be equipped with pretreatment pool, advanced oxidation pond, coagulative precipitation tank, biochemistry pool, sludge concentration tank and sets
Preparation area, the pretreatment tank are divided into the first dosing pond, the second dosing pond and third dosing pond, the first dosing pond from top to bottom
It is connected with the second dosing pond, the second dosing pond is connected with third dosing pond, and medicine machine is placed in the battery limits, is wriggled
Waste water is drawn into the first dosing by pump, suction filter pump, control panel, aerator, chlorination equipment and filter device, the peristaltic pump
In pond, the waste water into the first dosing pond flows into the second dosing pond and third dosing pond successively, is then added by being arranged on third
The first aperture on medicine pond flows into advanced oxidation pond, into advanced oxidation pond waste water by be arranged on advanced oxidation pond the
Two apertures flow into coagulative precipitation tank, are settled in coagulative precipitation tank, the supernatant of waste water is by being arranged on coagulation after sedimentation
Downflow weir on sedimentation basin is flowed into biochemistry pool, completes by suction filter pump to be drawn into filter device after reaction in biochemistry pool filtered
Chlorination equipment is flowed into afterwards to be disinfected after discharge, the control panel control medicine machine to the first dosing pond, the second dosing pond and
Dosing in third dosing pond, the aerator are supplied oxygen into biochemistry pool, and the sludge concentration tank is collecting pretreatment pool, mixed
Sludge in solidifying sedimentation basin and biochemistry pool.
2. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that added in the first dosing pond
Liquid is adjusted to adjust the pH of waste water acid-base value, aluminium polychloride or demulsifier, the third are added in the second dosing pond
It is added in dosing pond to adsorb the polyacrylamide of the suspended particulate in waste water, is also placed in the second dosing pond
Except the second tilted plate separator of the suspended particulate in waste water.
3. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that biology is placed in the biochemistry pool
Filler and membrane module, the biologic packing material is biodegradable to be carried out to waste water, and the membrane module is to having in filtered wastewater
Machine object.
4. vehicle moving sewage treatment equipment as claimed in claim 3, which is characterized in that the biologic packing material selects fiber
Any one of beam, fibrous nodules, cotton ball or haydite, the membrane module are middle control tunica fibrosa or plate membrane, in the membrane module
Membrane component select any one of microfiltration membranes, ultrafiltration membrane or NF membrane.
5. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that held in the coagulative precipitation tank
To adsorb the polyacrylamide of the suspended particulate in waste water, and it is placed with to remove first of suspended particulate in waste water tiltedly
Plate settling vessel.
6. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that the advanced oxidation pond is iron carbon
Micro cell or Fenton oxidation electrolytic cell.
7. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that the filter device is multimedium
Filter or carbon filter.
8. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that the chlorination equipment passes through ultraviolet
Line carries out poisoning bacterium of going out to water.
9. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that the bottom in the first dosing pond
Equipped with third aperture, the first dosing pond is connected with the second dosing pond by third aperture, the bottom in the second dosing pond is set
There is the 4th aperture, connected in the second dosing pond with third dosing pond by the 4th aperture.
10. vehicle moving sewage treatment equipment as described in claim 1, which is characterized in that the pretreatment tank is to waste water
It carries out water quality adjustment and sedimentation obtains first order processing waste water, after flowing into advanced oxidation pond oxygen occurs for the first order processing waste water
Second level processing waste water is obtained by the reaction in change, and the second level processing waste water flows into coagulative precipitation tank and realizes mud-water separation, obtains
Clear liquid, the supernatant carry out biodegradable and UF membrane after being flowed into biochemistry pool, obtain third level processing waste water, the third
Grade processing waste water is further across the water purification that discharge standard must be reached after the filtering of filter device, chlorination equipment disinfection.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201711483996.6A CN108191150A (en) | 2017-12-29 | 2017-12-29 | A kind of vehicle moving sewage treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201711483996.6A CN108191150A (en) | 2017-12-29 | 2017-12-29 | A kind of vehicle moving sewage treatment equipment |
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| CN108191150A true CN108191150A (en) | 2018-06-22 |
Family
ID=62587103
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| CN201711483996.6A Pending CN108191150A (en) | 2017-12-29 | 2017-12-29 | A kind of vehicle moving sewage treatment equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110651752A (en) * | 2019-10-09 | 2020-01-07 | 广州自然传奇生态环境科技有限公司 | Water quality circulating purification and oxygen supply device for aquaculture pond |
| CN112645552A (en) * | 2020-11-26 | 2021-04-13 | 江苏建筑职业技术学院 | Silt is administered with silt solidification equipment that can two-way pay-off |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140332450A1 (en) * | 2007-08-01 | 2014-11-13 | Rockwater Resource, LLC | Mobile station for diagnosing and modeling site specific effluent treatment facility requirements |
| CN204981518U (en) * | 2015-09-14 | 2016-01-20 | 常州市新港热电有限公司 | Wastewater recovery high efficient regeneration system |
| CN206014608U (en) * | 2016-08-24 | 2017-03-15 | 深圳市福田区环境技术研究所有限公司 | A kind of vehicle-mounted integral oil-containing waste water treating device |
| CN106554129A (en) * | 2015-09-25 | 2017-04-05 | 上海凡清环境工程有限公司 | Integral synchronous nitration denitrification sewage-treatment plant |
| CN206244613U (en) * | 2016-12-12 | 2017-06-13 | 厦门爱迪特环保科技有限公司 | A kind of printing and dyeing wastewater treatment system |
| CN206428125U (en) * | 2017-01-10 | 2017-08-22 | 北京奥达星环境工程有限公司 | A kind of portable sewage disposal system |
| CN206447734U (en) * | 2017-01-17 | 2017-08-29 | 杭州华测检测技术有限公司 | A kind of combined type sewage treatment equipment |
| CN107176749A (en) * | 2016-03-11 | 2017-09-19 | 浙江国清环保科技有限公司 | Integral continuous Fenton oxidation-reduction sewage disposal device |
-
2017
- 2017-12-29 CN CN201711483996.6A patent/CN108191150A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140332450A1 (en) * | 2007-08-01 | 2014-11-13 | Rockwater Resource, LLC | Mobile station for diagnosing and modeling site specific effluent treatment facility requirements |
| CN204981518U (en) * | 2015-09-14 | 2016-01-20 | 常州市新港热电有限公司 | Wastewater recovery high efficient regeneration system |
| CN106554129A (en) * | 2015-09-25 | 2017-04-05 | 上海凡清环境工程有限公司 | Integral synchronous nitration denitrification sewage-treatment plant |
| CN107176749A (en) * | 2016-03-11 | 2017-09-19 | 浙江国清环保科技有限公司 | Integral continuous Fenton oxidation-reduction sewage disposal device |
| CN206014608U (en) * | 2016-08-24 | 2017-03-15 | 深圳市福田区环境技术研究所有限公司 | A kind of vehicle-mounted integral oil-containing waste water treating device |
| CN206244613U (en) * | 2016-12-12 | 2017-06-13 | 厦门爱迪特环保科技有限公司 | A kind of printing and dyeing wastewater treatment system |
| CN206428125U (en) * | 2017-01-10 | 2017-08-22 | 北京奥达星环境工程有限公司 | A kind of portable sewage disposal system |
| CN206447734U (en) * | 2017-01-17 | 2017-08-29 | 杭州华测检测技术有限公司 | A kind of combined type sewage treatment equipment |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110651752A (en) * | 2019-10-09 | 2020-01-07 | 广州自然传奇生态环境科技有限公司 | Water quality circulating purification and oxygen supply device for aquaculture pond |
| CN112645552A (en) * | 2020-11-26 | 2021-04-13 | 江苏建筑职业技术学院 | Silt is administered with silt solidification equipment that can two-way pay-off |
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