CN109626709A - River water body comprehensive purifying processing system - Google Patents
River water body comprehensive purifying processing system Download PDFInfo
- Publication number
- CN109626709A CN109626709A CN201811343626.7A CN201811343626A CN109626709A CN 109626709 A CN109626709 A CN 109626709A CN 201811343626 A CN201811343626 A CN 201811343626A CN 109626709 A CN109626709 A CN 109626709A
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- Prior art keywords
- water
- zone
- water body
- plate
- dissolving
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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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
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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
- 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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/109—Characterized by the shape
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
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)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a kind of river water body comprehensive purifying processing system, including water body lifting device, water depth processing unit, air floatation machine and automatic oxygen-dissolving apparatus, setting biologic packing material is used to remove the COD and total phosphorus in water body in water depth processing unit；The air floatation machine includes cabinet and dissolving, contact zone, Disengagement zone, clear water zone and settling zone are disposed in cabinet, contact zone is provided with molten gas release head, molten gas release head connects dissolving, in Disengagement zone bottom, bucket is set, setting Slag Scraping Device and scraper plate above Disengagement zone, clear water zone are arranged reflux line and are connected to dissolving；The water outlet of the air floatation machine is connected to automatic oxygen-dissolving apparatus again, and to treated, water body carries out dissolved oxygen to automatic oxygen-dissolving apparatus.Processing system of the invention can targetedly remove the organic and inorganic pollution in river water, improve the light transmittance of water body, and water outlet dissolved oxygen DO may be up to 8.0mg/L or more.
Description
Technical field
The present invention relates to river regulation fields, and in particular to river water body comprehensive purifying processing system.
Background technique
Long river river ecological function is weak, and is discharged into phenomenon there are all kinds of lives, Fishery Pollution source, river water quality status according to
It so allows of no optimist, river bottom mud blacks, and has Mud up-floating situation, and water body is in blackish green, poor fluidity, low visibility；In water
Suspended matter and floater are more, and are easy to be deposited on bottom riverbed and form a large amount of bed muds, the pollution being enriched in bed mud
Substance is easily re-released into water body and forms endogenous pollution.
Pollution source is divided into endogenous pollution and external source pollution.Endogenous pollution is mainly that the pollutant release of river bottom mud is made
At some water body flows are poor, and the pollutant in river water is easily deposited on river bed, become bed mud, will be dirty in water body exchange
Dye object is re-released into the endogenous pollution in water body and foring river.External source pollution is mainly due to sanitary sewage, Waste
The extraneous contamination of the formation such as water, rainfall, rubbish object causes
Summary of the invention
The technical problem to be solved by the present invention is to the existing one kind that provides can integrate to smelly, nigrescence river water body
The purification system of processing.
In order to solve the above-mentioned technical problem, a kind of the technical solution adopted by the present invention are as follows: river water body comprehensive purifying processing
System, including water body lifting device, water depth processing unit, air floatation machine and automatic oxygen-dissolving apparatus, water body lifting device will
River water body is promoted and is delivered in water depth processing unit, and setting biologic packing material is used in water depth processing unit
Remove the COD and total phosphorus in water body；The air floatation machine includes cabinet and dissolving, and the first contact is disposed in cabinet
Area, the first Disengagement zone, clear water zone, the second Disengagement zone, the second contact zone and settling zone, in the first contact zone and the second contact zone
It is provided with molten gas release head, molten gas release head connects dissolving, bucket is arranged in Disengagement zone bottom, setting is scraped above Disengagement zone
Slag machine and scraper plate, clear water zone are arranged reflux line and are connected to dissolving；The water outlet of the air floatation machine is connected to automatic dissolved oxygen dress again
It sets, to treated, water body carries out dissolved oxygen to automatic oxygen-dissolving apparatus.
Further, the water depth processing unit includes contact-oxidation pool and multiphase loop module, in catalytic oxidation
Bottom of pond portion is provided with microporous aeration disc, and suspension type filler, the bottom of the multiphase loop module are additionally provided in contact-oxidation pool
Portion is connected to in contact-oxidation pool, and the multiphase loop module includes carriage body, and biologic packing material plate and exposure are provided in carriage body
Device of air, the aerator, which is used to for the sewage of multiphase loop module bottom being up-shifted in air, to be fallen after rise after aeration to life
Object filler plate, biologic packing material plate is in honeycomb and is obliquely installed, and its surface is provided with multiple lug bosses and is used for area increased,
Reflux pump is additionally provided with below multiphase loop module, reflux pump connects reflux line for the sewage by the processing of multiphase loop module
It is back to contact-oxidation pool, car top is provided with liquid discharge outlet, and multiple support columns are provided with below carriage body for holding up
Carriage body, the scalable setting of support column, is additionally provided with sludge pipe in multiphase loop module.
Further, the aerator includes air lift water pipe and umbrella aeration head, and air lift water pipe is vertically arranged and stretches out
Carriage body bottom, umbrella aeration are arranged on air lift water pipe and are located above biologic packing material plate；It is also provided with below biologic packing material plate
There is aeration plate.
Further, the molten gas release head includes tube body, bubble liquid gas input channel is arranged in tube body, in bubble liquid gas
Input channel front end is provided with drainage plate and forms tapered channel, and drainage front edge of board is provided with reflecting plate, reflecting plate and drainage plate
Between, between reflecting plate and inboard wall of tube body be provided with gap, reflecting plate is provided with tapered recess close to the end of drainage plate,
Other end outer peripheral surface is also tapered, and tapered recess is coaxially set with tube body, and gap forms rotation between reflecting plate and drainage plate
Turn trough.
Processing system of the invention can targetedly remove the organic and inorganic pollution in river water, improve water
The light transmittance of body, water outlet dissolved oxygen DO may be up to 8.0mg/L or more.
Detailed description of the invention
Fig. 1 is functional block diagram of the invention；
Fig. 2 is the structural schematic diagram of water depth processing unit in the present invention；
Fig. 3 is the structural schematic diagram of biologic packing material plate in the present invention；
Fig. 4 is the structural schematic diagram of air floatation machine in the present invention；
Fig. 5 is the structural schematic diagram of molten gas release head in the present invention.
Specific embodiment
A specific embodiment of the invention is illustrated below in conjunction with attached drawing.
It elaborates below in conjunction with specific embodiment of the attached drawing to invention.
As shown in Figure 1, river sewage comprehensive purifying processing system of the invention, including water body lifting device 1, water depth
River water body is promoted and is delivered to water by processing unit 2, air floatation machine 3 and automatic oxygen-dissolving apparatus 4, water body lifting device 1
In body advanced treatment apparatus, mainly form by elevator pump, suspension arrangement, grid and with circuits etc..
Setting biologic packing material is used to remove the pollutants such as COD, TP in water body in water depth processing unit, specific to tie
Structure is as shown in Figures 2 and 3 comprising contact-oxidation pool 22 and multiphase loop module 212,22 bottom of contact-oxidation pool are provided with micro-
Hole aeration plate 211 is provided with suspension type filler 210 in contact-oxidation pool, and waste water is after leading portion pretreatment and Anaerobic Treatment
Into the sewage disposal system.Debugging initial stage lacks dominant microflora in system.Sewage carries out of short duration first in contact-oxidation pool
Stop oxygenation mixing is rapidly carried out by the aeration effect of microporous aeration disc.
The bottom of multiphase loop module 212 is connected to in contact-oxidation pool, naturally it is also possible to directly by multiphase loop module
Be directly embedded in contact-oxidation pool, multiphase loop module includes carriage body 23, be provided in carriage body 23 biologic packing material plate 28 with
And aerator, the aerator is used to for the sewage of multiphase loop module bottom being up-shifted in air to be fallen after rise after aeration
To biologic packing material plate 28, biologic packing material plate 28 is in honeycomb and is obliquely installed.Cellular filler plate biofilm rate is high, can basis
Sewage quality generates rapidly a large amount of dominant microfloras, and by the air lift of aerator, ringing, dominant bacteria is diffused to whole
In a sewerage, accelerate the starting rate of whole system.In normal operation, under the action of aerator, sewage is by bottom
It rises in air, then falls and return in sewage disposal system, which is repeated, and increases stop of the sewage in system
Time.COD, BOD in microorganism fully degraded sewage enhance wastewater treatment efficiency, and the module is but also as sloping plate deposition
Carrier reduces the load in post precipitation pond, while most of sludge is retained in modified form biological tank, improves in biological tank
Microorganism concn, not only improve the treatment effect of sewage, sludge reduction also made by the aerobic sigestion of organic sludge, drop
Low sludge discharge.The surface of filler plate 8 is additionally provided with multiple lug bosses 13 for area increased, as shown in Figure 3.
Reflux pump 27 is additionally provided with below multiphase loop module, reflux pump 27 connects reflux line 21 and will follow by multiphase
For the sewage backflow of ring resume module to contact-oxidation pool 22, car top is provided with liquid discharge outlet 26, is arranged below carriage body
There are multiple support columns 29 that can realize using air cylinder structure for holding up carriage body, the scalable setting of support column 29, support column
Smoothly lifting.The structure can change the gap below biologic packing material plate, keep sewage largely in the gap, and keep away
Exempt from liquid level and covers aerator.Sludge pipe (being not drawn into figure) is additionally provided in multiphase loop module.
Aerator includes air lift water pipe 25 and umbrella aeration head 24, and air lift water pipe is vertically arranged and stretches out carriage body bottom
Portion extracts bottom sewage and getting into the air by umbrella aeration head and is aerated, then fallen after rise to biological modulated flitch, progress
Microbial degradation, umbrella aeration are arranged on air lift water pipe and are located above biologic packing material plate.In order to increase aeration efficiency, in life
Aeration plate is also equipped with below object filler plate.
As shown in figure 4, air floatation machine 3 includes cabinet 32 and dissolving 31, the first contact zone is disposed in cabinet 31
35, the first Disengagement zone, clear water zone 37, the second Disengagement zone, the second contact zone 36 and settling zone 28, in the first contact zone and second
Contact zone is provided with molten gas release head 39, and molten gas release head 39 connects dissolving, and bucket 34, separation is arranged in Disengagement zone bottom
Setting Slag Scraping Device and scraper plate above area, clear water zone are arranged reflux line 33 and are connected to dissolving；The water outlet of the air floatation machine is again
It is connected to automatic oxygen-dissolving apparatus, water body carries out dissolved oxygen to automatic oxygen-dissolving apparatus to treated.
The specific structure of dissolved oxygen release head is as shown in figure 5, included tube body 391, the interior setting bubble liquid gas of tube body 391 input
Channel 392 is provided with drainage plate 393 in 392 front end of bubble liquid gas input channel and forms tapered channel, in drainage front edge of board setting
There is reflecting plate 395, between reflecting plate and drainage plate, is provided with gap between reflecting plate and inboard wall of tube body, reflecting plate 395 is close
The end of drainage plate is provided with tapered recess 395, and other end outer peripheral surface is also tapered, and tapered recess is set with tube body coaxial line
It sets, gap forms swivelling chute between reflecting plate and drainage plate.Microbubble liquid air-flow is squeezed in liquid cyclone turn trough, rotates, is cut
It projects to form nano bubble through nano bubble relief hole, pipe is discharged by nano bubble and enters flotation tank.
In entire process flow end, automatic oxygen-dissolving apparatus is set.By water purifying device and water depth processing unit
Two-stage process treated processing water outlet, by importing out automatic oxygen-dissolving apparatus, from its overflow hole flow into natural water.Automatic dissolving
Oxygen device is overflow by having the overflow hole of certain roughness on the surface that water outlet is arranged to improve the dynamic characteristics of water body
So that processing water outlet is flowed into the form of thread, the specific surface area that increase is contacted with air improves dissolved oxygen for the setting of discharge orifice.
The guarantee of dissolved oxygen and mobility is increased for the rear end self-purification of water.Meanwhile promoting environmental landscape feature.
This system can realize that existing COD is reduced to 20mg/L by 50mg/L, up to 60% removal rate；Realize total phosphorus by 1mg/L
It is reduced to 0.08mg/L, up to 90% or more removal rate；Water transparency handles the 1.5m in later period by increasing to less than 50cm, thus
It realizes from black smelly water and is changed into limpid water body.
Claims (4)
1. a kind of river water body comprehensive purifying processing system, it is characterised in that: including water body lifting device, water depth processing dress
It sets, river water body is promoted and is delivered to water depth processing by air floatation machine and automatic oxygen-dissolving apparatus, water body lifting device
In device, setting biologic packing material is used to remove the COD and total phosphorus in water body in water depth processing unit；The air floatation machine packet
Cabinet and dissolving are included, the first contact zone, the first Disengagement zone, clear water zone, the second Disengagement zone, second are disposed in cabinet
Contact zone and settling zone are provided with molten gas release head in the first contact zone and the second contact zone, and molten gas release head connection is molten
Bucket, setting Slag Scraping Device and scraper plate above Disengagement zone is arranged in Disengagement zone bottom in gas tank, and clear water zone is arranged reflux line and is connected to
Dissolving；The water outlet of the air floatation machine is connected to automatic oxygen-dissolving apparatus again, and water body progress is molten to treated for automatic oxygen-dissolving apparatus
Oxygen.
2. river water body comprehensive purifying processing system according to claim 1, it is characterised in that: the water depth processing
Device includes contact-oxidation pool and multiphase loop module, catalytic oxidation bottom of pond portion is provided with microporous aeration disc, in catalytic oxidation
Suspension type filler is additionally provided in pond, the bottom of the multiphase loop module is connected to in contact-oxidation pool, the multiphase circulation
Module includes carriage body, biologic packing material plate and aerator is provided in carriage body, the aerator is for recycling multiphase
The sewage of module bottom, which is up-shifted in air after aeration, to be fallen after rise to biologic packing material plate, and biologic packing material plate is in honeycomb and inclination
Setting, and its surface is provided with multiple lug bosses for area increased, is additionally provided with reflux pump below multiphase loop module, returns
For stream pump connection reflux line by the sewage backflow by the processing of multiphase loop module to contact-oxidation pool, car top is provided with liquid
Body discharge outlet is provided with multiple support columns for holding up carriage body, the scalable setting of support column, in multiphase cyclic module below carriage body
Sludge pipe is additionally provided in block.
3. river water body comprehensive purifying processing system according to claim 2, it is characterised in that: the aerator includes
Air lift water pipe and umbrella aeration head, air lift water pipe are vertically arranged and stretch out carriage body bottom, and umbrella aeration is arranged in air lift water pipe
Above and it is located above biologic packing material plate；Aeration plate is also equipped with below biologic packing material plate.
4. river water body comprehensive purifying processing system according to claim 1, it is characterised in that: the molten gas release head packet
Tube body is included, bubble liquid gas input channel is set in tube body, bubble liquid gas input channel front end is provided with drainage plate and forms taper
Channel is provided with reflecting plate in drainage front edge of board, is provided between reflecting plate and drainage plate, between reflecting plate and inboard wall of tube body
Gap, reflecting plate are provided with tapered recess close to the end of drainage plate, and other end outer peripheral surface is also tapered, tapered recess with
Tube body is coaxially set, and gap forms swivelling chute between reflecting plate and drainage plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811343626.7A CN109626709A (en) | 2018-11-13 | 2018-11-13 | River water body comprehensive purifying processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811343626.7A CN109626709A (en) | 2018-11-13 | 2018-11-13 | River water body comprehensive purifying processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109626709A true CN109626709A (en) | 2019-04-16 |
Family
ID=66067788
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811343626.7A Pending CN109626709A (en) | 2018-11-13 | 2018-11-13 | River water body comprehensive purifying processing system |
Country Status (1)
| Country | Link |
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| CN (1) | CN109626709A (en) |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2062728U (en) * | 1990-03-16 | 1990-09-26 | 谢绍舜 | Integrated biochemistry processor for sewage |
| CN1618744A (en) * | 2003-11-19 | 2005-05-25 | 彭云龙 | River late water purification method and its special flowing aeration equipment |
| CN101293722A (en) * | 2008-06-20 | 2008-10-29 | 云南天兰环保科技开发有限公司 | Municipal sewage treatment system and equipment built on river |
| CN101426736A (en) * | 2006-04-10 | 2009-05-06 | 美多拉环保公司 | Water circulation systems for ponds, lakes, municipal tanks, and other bodies of water |
| CN101830533A (en) * | 2010-05-31 | 2010-09-15 | 哈尔滨工业大学 | V-shaped air floating filter with deslagging function |
| CN102372399A (en) * | 2011-09-29 | 2012-03-14 | 河南中烟工业有限责任公司 | Sewage treatment process |
| CN102774921A (en) * | 2012-08-15 | 2012-11-14 | 北京英特环科水处理工程设备有限公司 | Nanometer (NM) gas floating system device |
| CN105540825A (en) * | 2016-02-03 | 2016-05-04 | 江西省三余环保节能科技有限公司 | Fiber bundle bioreactor for sewage treatment |
| CN205275343U (en) * | 2015-11-11 | 2016-06-01 | 江苏华达环境工程有限公司 | Odd -numbered day is handled and is greater than 150 tons air supporting all -in -one |
| CN207774896U (en) * | 2017-12-26 | 2018-08-28 | 上海双骏环保科技有限公司 | A kind of biochemistry pool gasket packing fixing device |
-
2018
- 2018-11-13 CN CN201811343626.7A patent/CN109626709A/en active Pending
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|---|---|---|---|---|
| CN2062728U (en) * | 1990-03-16 | 1990-09-26 | 谢绍舜 | Integrated biochemistry processor for sewage |
| CN1618744A (en) * | 2003-11-19 | 2005-05-25 | 彭云龙 | River late water purification method and its special flowing aeration equipment |
| CN101426736A (en) * | 2006-04-10 | 2009-05-06 | 美多拉环保公司 | Water circulation systems for ponds, lakes, municipal tanks, and other bodies of water |
| CN101293722A (en) * | 2008-06-20 | 2008-10-29 | 云南天兰环保科技开发有限公司 | Municipal sewage treatment system and equipment built on river |
| CN101830533A (en) * | 2010-05-31 | 2010-09-15 | 哈尔滨工业大学 | V-shaped air floating filter with deslagging function |
| CN102372399A (en) * | 2011-09-29 | 2012-03-14 | 河南中烟工业有限责任公司 | Sewage treatment process |
| CN102774921A (en) * | 2012-08-15 | 2012-11-14 | 北京英特环科水处理工程设备有限公司 | Nanometer (NM) gas floating system device |
| CN205275343U (en) * | 2015-11-11 | 2016-06-01 | 江苏华达环境工程有限公司 | Odd -numbered day is handled and is greater than 150 tons air supporting all -in -one |
| CN105540825A (en) * | 2016-02-03 | 2016-05-04 | 江西省三余环保节能科技有限公司 | Fiber bundle bioreactor for sewage treatment |
| CN207774896U (en) * | 2017-12-26 | 2018-08-28 | 上海双骏环保科技有限公司 | A kind of biochemistry pool gasket packing fixing device |
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|---|
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Application publication date: 20190416 |
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| RJ01 | Rejection of invention patent application after publication |