CN206705899U - Integrated depth-averaged model equipment - Google Patents
Integrated depth-averaged model equipment Download PDFInfo
- Publication number
- CN206705899U CN206705899U CN201720294676.5U CN201720294676U CN206705899U CN 206705899 U CN206705899 U CN 206705899U CN 201720294676 U CN201720294676 U CN 201720294676U CN 206705899 U CN206705899 U CN 206705899U
- Authority
- CN
- China
- Prior art keywords
- model equipment
- depositing reservoir
- integrated depth
- averaged model
- equipment according
- 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.)
- Active
Links
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a kind of integrated depth-averaged model equipment, including the reaction tank, depositing reservoir and clear water reserviors being sequentially connected, the reaction tank is provided with water inlet, the clear water reserviors are provided with delivery port, baffle plate is provided between the reaction tank and the depositing reservoir, some filters being sequentially connected are provided with the depositing reservoir, the filter includes support and the micropore filter cloth being fixed on support.Handled by integrated depth-averaged model equipment to water body total suspended solid clearance height, and combined according to different quality and add other water eutrophication indexs such as corresponding biological bacteria removable phosphorus, ammonia nitrogen, COD, heavy metal removal is preferable.
Description
Technical field
A kind of integrated depth-averaged model equipment is the utility model is related to, for Treated sewage reusing, circulating water treatment, air supporting work
The water treatment fields such as mark, municipal wastewater, Industry Waste water extraction mark are put forward after skill.
Background technology
Existing water treatment facilities operating cost is high, floor space is big, if big flow processing needs to change civil engineering structure, area
Greatly, long construction period, dilatation inconvenience.
Traditional filter tank valve is relatively more, and general big resistance is rinsed, it is necessary to be provided with flushing device；And the grain-by-grain seed selection of filtrate footpath select compared with
Strictly；Require high during flushing, often occur to run material phenomenon because filtrate grain falls short of specifications；Easy deposition between filtrate；Sand removal is more not
It is convenient；Dosing complex management；Work period is shorter.
Utility model content
It is few, high to water body total suspended solid clearance that problem to be solved in the utility model is to provide a kind of auxiliary device
Integrated depth-averaged model equipment.
In order to solve the above-mentioned technical problem, the utility model adopts the following technical scheme that：
Integrated depth-averaged model equipment, including reaction tank, depositing reservoir and the clear water reserviors being sequentially connected, the reaction tank are set
There is water inlet, the clear water reserviors are provided with delivery port, are provided with baffle plate between the reaction tank and the depositing reservoir, in the depositing reservoir
Provided with some filters being sequentially connected, the filter includes support and the micropore filter cloth being fixed on support.
Preferably, the support is that the hollow tube that through hole is disposed with tube wall is formed.
Preferably, connected between the filter by collector pipe, the both ends of the collector pipe fill with two filterings respectively
The hollow tube docking put.
Preferably, it is provided with mud-sucking device in the depositing reservoir.
Preferably, the mud-sucking device includes the dredging tube inhaled mud driving and be fixed in the suction mud driving, the suction
Mud driving is provided with dredge pump positioned at the middle part of depositing reservoir, the suction mud driving.
Preferably, the dredging tube has two, and two dredging tubes are located at the bottom and top of the depositing reservoir respectively.
Preferably, the bottom of the depositing reservoir is provided with recoil tube.
Preferably, the reaction tank is connected with feeding device.
Preferably, high polymer coagulant is stored in the feeding device.
Handled by integrated depth-averaged model equipment to water body total suspended solid clearance height, and according to difference
Water quality, which combines, adds other water eutrophication indexs such as corresponding biological bacteria removable phosphorus, ammonia nitrogen, COD (COD), counterweight
Metal removal is preferable.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model integration depth-averaged model equipment；
Fig. 2 is the top view of depositing reservoir.
Embodiment
As depicted in figs. 1 and 2, integrated depth-averaged model equipment, including two reaction tanks being sequentially connected 1, one are clear
Clear pond 2 and a clear water reserviors 3, the reaction tank are provided with water inlet 4, and the clear water reserviors are provided with delivery port 5, the reaction tank 1 and
Baffle plate is provided between the depositing reservoir 2, the reaction tank is connected to feeding device 12, height is stored in the feeding device
Molecular flocculant.Some filters being sequentially connected are provided with the depositing reservoir, the filter includes support 6 and fixed
Micropore filter cloth 7 on support.The bottom of the depositing reservoir is provided with recoil tube 8.
The support of filter is formed using the hollow tube that through hole is disposed with tube wall.Pass through collection between the filter
Water pipe 9 connects, and the hollow tube of the both ends of the collector pipe respectively with two filters docks.
Mud-sucking device is provided with the depositing reservoir 2.The mud-sucking device includes inhaling mud driving 10 and is fixed on the suction mud
Dredging tube 11 in driving, described to inhale mud driving positioned at the middle part of depositing reservoir 2, the suction mud, which is driven a vehicle, is provided with dredge pump.The suction
Mud pipe 11 has two, and two dredging tubes 11 are located at the bottom and top of the depositing reservoir 2 respectively.
In use, sewage enters the operation pretreatment of big flow Multifunctional water treatment equipment first, then water outlet enters this reality
With the new integrated depth-averaged model equipment, reaction tank is flocculated into flco by high polymer coagulant, and overflow filter tank is through gear
After plate, by the micropore filter cloth being fixed on support, solid suspension is trapped within the outside of filter cloth, and filtered fluid is received by hollow tube
Collection, gravity stream discharge filter tank by overflow launder.In filtering, sludge absorption gradually forms sludge blanket, with filter cloth on the outside of filter cloth
The accumulation of upper sludge, filter-cloth filtering resistance increase, and liquid level gradually rises in pond, when discharge pressure rises to setting value, PLC
(programmable controller) while dredge pump and transmission device are opened, proceed by negative-pressure irrigation：Vertical filter disc is fixed, mobile
Rinse driving and dredge pump start, start to carry out wire scan-type to the flco of filter surface load to inhale and washes, the muddy water of sucking-off by
Outside dredge pump device for transferring, back purge system operation finishes, and the filter cloth after cleaning immediately enters filtration condition.
Whole equipment simple and compact, auxiliary device is few, and the investment of whole filtration system is low, can continuously filter (conventional sand filtration
To realize continuous filtering, intermediate pool or more alternations need to be set before sand filter).And floor space is small.Identical
Treatment scale and the rate of filtration under, filtering cloth filtering pool floor space is only the 1/2 of conventional gas-water backwash filtration, has been saved a large amount of
Cost of land.
The advantages of the utility model：
1st, innovative design is employed, filter disc is easily changed；
2nd, scan-type purging system, cleaning efficiency is improved, extends the service life of filter cloth；
3rd, low SS (suspension) concentration can be effectively removed, clearance adds corresponding life up to more than 75%, while in reaction tank
Also CODcr, BOD5 (five days biochemical oxygen demand) and TP (total phosphorus) concentration can be reduced after thing bacterium；
Negative-pressure ward mode is used when the 4th, being cleaned due to filter cloth, it is not necessary to back suction priming reservoir, effluent quality can be greatly improved；
5th, energy consumption is saved.Its folk prescription processing energy consumption is only 0.0012 (degree electricity/m3), it is conventional gas-water backwash filtration energy consumption
1/3；
6th, filtering cloth head is small.Water head loss by filtration is up to 0.31m, and conventional gas-water backwash filtration filtering cloth head is more than
2.0m, reclaimed water lifting lift is saved；For grassroot project, lifting device and lifting structures can be cancelled；
7th, filter cycle is long, Clean after every is long, cleaning lasts short, and waterpower and sludge loading are much larger than conventional sand filtration；
8th, in the absence of growth film the problem of, it is not necessary to chlorination measure before taking；When processing SS is only required in water inlet, can save
Go dosing link；
9th, floor space is small.Under identical treatment scale and the rate of filtration, filtering cloth filtering pool floor space is only conventional
The 1/2 of gas-water backwash filtration, substantial amounts of cost of land is saved, there is significant advantage in modernizing and expanding the existing factory；
10th, filter cloth filter is easily installed than pellet filter tank.After joint connection in site pipe fitting and electrical equipment, you can input
Use.And pellet filter tank then generally requires to carry out filtrate installation；
11st, operation automation, thus run and safeguard simply, conveniently.Due to relatively few, the main rapid wear of its moving component
Part filter cloth also only needs 5 years one to change, and maintenance workload is small, while whole filter tank employs PLC automatic control system, operation letter
It is single, it is easy to use；
12nd, design cycle and short construction period.Filter cloth filter integral device, can integrally it ship, design and construction party
Just it is and quick；And enlarging is easy；
13rd, simple and compact device, auxiliary device is few, and the investment of whole filtration system is low, can continuously filter (if conventional sand filtration
Continuous filtering is realized, intermediate pool or more alternations need to be set before sand filter).
Claims (9)
1. integrated depth-averaged model equipment, it is characterised in that：Including the reaction tank, depositing reservoir and clear water reserviors being sequentially connected, institute
State reaction tank and be provided with water inlet, the clear water reserviors are provided with delivery port, and baffle plate, institute are provided between the reaction tank and the depositing reservoir
State and some filters being sequentially connected are provided with depositing reservoir, the filter includes support and the micropore being fixed on support
Filter cloth.
2. integrated depth-averaged model equipment according to claim 1, it is characterised in that：The support is to be arranged on tube wall
The hollow tube for having through hole is formed.
3. integrated depth-averaged model equipment according to claim 2, it is characterised in that：Pass through between the filter
Collector pipe connects, and the hollow tube of the both ends of the collector pipe respectively with two filters docks.
4. integrated depth-averaged model equipment according to claim 1, it is characterised in that：It is provided with the depositing reservoir and inhales mud
Device.
5. integrated depth-averaged model equipment according to claim 4, it is characterised in that：The mud-sucking device includes inhaling mud
The dredging tube driven a vehicle and be fixed in the suction mud driving, it is described to inhale mud driving positioned at the middle part of depositing reservoir, the suction mud driving
Provided with dredge pump.
6. integrated depth-averaged model equipment according to claim 5, it is characterised in that：The dredging tube has two, and two
Dredging tube described in root is located at the bottom and top of the depositing reservoir respectively.
7. integrated depth-averaged model equipment according to claim 1, it is characterised in that：The bottom of the depositing reservoir is provided with
Recoil tube.
8. integrated depth-averaged model equipment according to claim 1, it is characterised in that：The reaction tank is connected with charging
Device.
9. integrated depth-averaged model equipment according to claim 8, it is characterised in that：Stored in the feeding device
The high polymer coagulant of charging.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720294676.5U CN206705899U (en) | 2017-03-24 | 2017-03-24 | Integrated depth-averaged model equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720294676.5U CN206705899U (en) | 2017-03-24 | 2017-03-24 | Integrated depth-averaged model equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206705899U true CN206705899U (en) | 2017-12-05 |
Family
ID=60470136
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720294676.5U Active CN206705899U (en) | 2017-03-24 | 2017-03-24 | Integrated depth-averaged model equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206705899U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108525396A (en) * | 2018-04-28 | 2018-09-14 | 江苏灵氟隆环境工程有限公司 | A kind of automation filter cloth cleaning device |
-
2017
- 2017-03-24 CN CN201720294676.5U patent/CN206705899U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108525396A (en) * | 2018-04-28 | 2018-09-14 | 江苏灵氟隆环境工程有限公司 | A kind of automation filter cloth cleaning device |
| CN108525396B (en) * | 2018-04-28 | 2019-08-27 | 江苏灵氟隆环境工程有限公司 | A kind of automation filter cloth cleaning device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103922506B (en) | Integrated complete equipment for water quality purification treatment | |
| CN102626564A (en) | Novel multimedium filter for water treatment | |
| CN202625977U (en) | Purification and recycling device for mine and sewage | |
| CN104710084B (en) | A kind of high-efficiency biomembrane integrated sewage treating apparatus | |
| CN210286897U (en) | Continuous alternating MBBR sewage treatment device | |
| CN205182284U (en) | Gravity type valveless filter | |
| CN206705899U (en) | Integrated depth-averaged model equipment | |
| CN206985861U (en) | A kind of livestock and poultry cultivation sewage disposal zero-emission and organic fertilizer recovery system | |
| CN102311171B (en) | Horizontal well sewage treatment plant and method thereof | |
| CN106865643A (en) | A kind of ceramic straight filter system for processing waste water of mine of not dosing | |
| CN208308648U (en) | Low energy consumption integrated sewage treating apparatus | |
| CN215975459U (en) | Small-size sewage treatment system of buried reinforced concrete structure entirely | |
| CN206188491U (en) | Membrane bioreactor that sewage sludge integration was handled | |
| CN110294568A (en) | One kind is for improveing UCT sewage treatment plant and method | |
| CN201148371Y (en) | Aluminum oxide industrial production wastewater treatment recycling apparatus | |
| CN101898853B (en) | Sewage primary sedimentation treatment method and system for removing intensified suspended solid inorganic component | |
| CN210764448U (en) | Oily sewage cleaning equipment | |
| CN212800031U (en) | Full-automatic car-washing wastewater circulating and purifying device | |
| CN209721764U (en) | A kind of sanitary sewage multi-stage filtration purifying device | |
| CN209797614U (en) | Sewage treatment reactor | |
| CN113577844A (en) | Water treatment suspended solid gets rid of and mud-water separation's sediment device | |
| CN112047577A (en) | Treatment system and process for underground water expression earth surface III of high-turbidity coal mine | |
| CN206915833U (en) | Waste Water Treatment | |
| CN208632333U (en) | Efficient printing and dyeing wastewater treatment system | |
| CN207259289U (en) | A kind of oily wastewater purification of water quality Environmental-protecting treater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |