CN206372699U - A kind of ultra-filtration membrane device continuously run without backwash pipeline - Google Patents
A kind of ultra-filtration membrane device continuously run without backwash pipeline Download PDFInfo
- Publication number
- CN206372699U CN206372699U CN201621478192.8U CN201621478192U CN206372699U CN 206372699 U CN206372699 U CN 206372699U CN 201621478192 U CN201621478192 U CN 201621478192U CN 206372699 U CN206372699 U CN 206372699U
- Authority
- CN
- China
- Prior art keywords
- water
- pipe
- tank
- pipeline
- inlet
- 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
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of ultra-filtration membrane device continuously run without backwash pipeline, including multiple hyperfiltration membrane assemblies, water inlet pipe, inlet water tank, automatic rotation blow-off pipe, water producing tank, recoil automatic rotary plate and water producing pipe, multiple hyperfiltration membrane assemblies are annularly distributed, water inlet pipe connects inlet water tank, inlet water tank connects multiple hyperfiltration membrane assembly water inlet ends by multiple pipeline A, water producing tank connects multiple hyperfiltration membrane assembly water sides by multiple pipeline B, automatic rotation blow-off pipe is arranged in inlet water tank, recoil automatic rotary plate is arranged in water producing tank, water producing pipe connects water producing tank, recoil automatic rotary plate is hollow cavity, two water inlets and a delivery port are at least offered above, automatic rotation blow-off pipe is sequentially communicated each hyperfiltration membrane assembly water inlet end, when hyperfiltration membrane assembly water inlet end is by rotation blow-off pipe connection automatically, the delivery port of water side connection recoil automatic rotary plate.The utility model can realize the backwash each other between hyperfiltration membrane assembly, can guarantee that the continuous operation of system.
Description
Technical field
The utility model is related to purifier field, and in particular to a kind of milipore filter dress continuously run without backwash pipeline
Put.
Background technology
According to the characteristics of ultra-filtration membrane device, all ultra-filtration membrane device operations are required to the operation for running, backwashing, reruning
Mode, so every group ultra-filtration membrane device (either modularization or single group) operation, is required for carrying out the conversion of the method for operation,
And it is both needed to the backwashing systems such as independent supporting back purge system, including backwashing pump, valve, pipeline, instrument, and such recoil
System pipeline is washed complicated, system is huge, cost of investment is high, power consumption is high, even if system, which is continuous operation, must also increase corresponding film
Heap and component are alternatively or standby, and can not change the process for shutting down backwash, are nominally " continuous operation ", essence is only
It is stopping and the start-up course of modular single group module, is not continuous operation truly.
The content of the invention
In view of this, it is necessary to provide between one kind can realize each hyperfiltration membrane assembly and backwash each other, and can continuously run
The ultra-filtration membrane device continuously run without backwash pipeline.
The technical solution adopted in the utility model:A kind of ultra-filtration membrane device continuously run without backwash pipeline, including it is multiple
Hyperfiltration membrane assembly, water inlet pipe, automatically inlet water tank, rotation blow-off pipe, water producing tank, recoil automatic rotary plate and water producing pipe, Duo Gesuo
State hyperfiltration membrane assembly to be annularly distributed, the water inlet pipe connects the inlet water tank, the inlet water tank connects many by multiple pipeline A
The individual hyperfiltration membrane assembly water inlet end, the water producing tank connects multiple hyperfiltration membrane assembly water sides, institute by multiple pipeline B
State automatic rotation blow-off pipe to be arranged in the inlet water tank, the recoil automatic rotary plate is arranged in the water producing tank, described
Water producing pipe connects the water producing tank, and the recoil automatic rotary plate is a hollow cavity, and two water inlets are at least offered above
With a delivery port, the automatic rotation blow-off pipe is sequentially communicated each hyperfiltration membrane assembly water inlet end, in the milipore filter
When component water inlet end is connected by the automatic rotation blow-off pipe, the delivery port of its water side connection recoil automatic rotary plate.
Compared with prior art, the utility model can directly pass through without independently setting up backwash pipeline, valve, water pump
Automatic rotation blow-off pipe is used cooperatively with recoil automatic rotary plate, you can realize the recoil each other between each hyperfiltration membrane assembly
Wash, and avoid itself damaging for the film equipment that existing system running is caused due to continual stop and start device
Bad, the particularly fracture of wire problem of film silk realizes the continuous operation of system, greatly reduces overall investment and the system of film equipment
Complexity, while adding the service life of film.
Brief description of the drawings
Fig. 1 show the attachment structure front view for the ultra-filtration membrane device continuously run without backwash pipeline in the utility model.
Fig. 2 show the attachment structure top view for the ultra-filtration membrane device continuously run without backwash pipeline in the utility model.
Embodiment
The utility model is further described below in conjunction with accompanying drawing, example is served only for explaining the utility model, and
It is non-to be used to limit scope of the present utility model.
As shown in Figure 1 and Figure 2, it is a kind of ultra-filtration membrane device 100 continuously run without backwash pipeline in the utility model, bag
Include multiple hyperfiltration membrane assemblies 10, water inlet pipe 20, inlet water tank 30, automatic rotation blow-off pipe 40, water producing tank 50, recoil automatic rotary plate
60 and water producing pipe 70.
The water inlet pipe 20 connects the inlet water tank 30, and the water producing pipe 70 connects the water producing tank 50, the inlet water tank
30 and the water producing tank 50 be cylindric casing.Multiple hyperfiltration membrane assemblies 10 are annularly distributed, and the inlet water tank 30 leads to
Cross multiple pipeline A80 and connect multiple water inlet ends of hyperfiltration membrane assembly 10, the water producing tank 50 connects many by multiple pipeline B90
The individual water side of the hyperfiltration membrane assembly 10, specifically, multiple pipeline A80 are placed equidistant in the side of the inlet water tank 30,
And multiple pipeline A80 and the inlet water tank 30 tie point are located at same level, multiple pipeline B90 are placed equidistant
In the side of the water producing tank 50, and multiple pipeline B90 and the tie point of the water producing tank 50 are located at same level, institute
State pipeline A80, the pipeline B90 and the three's quantity of the hyperfiltration membrane assembly 10 equal.The automatic rotation blow-off pipe 40 is set
In in the inlet water tank 30, further, the automatic rotation blow-off pipe 40 is rotated around the axis of the inlet water tank 30.It is described anti-
Rush automatic rotary plate 60 to be arranged in the water producing tank 50, further, the recoil automatic rotary plate 60 is around the water producing tank
50 axis is rotated.The recoil automatic rotary plate 60 is a hollow cavity, and overall curved, its external diameter is equal to the water producing tank
Two water inlets 61 and a delivery port are at least offered in 50 internal diameter, the arcuate flanks of the recoil automatic rotary plate 60
62, camber line between the adjacent water inlet 61 or the delivery port 62 distance be equal to the two neighboring pipeline B90 with it is described
Camber line distance between the tie point of water producing tank 50.The automatic rotation blow-off pipe 40 is in the axis rotation around the inlet water tank 30
During, each water inlet end of the hyperfiltration membrane assembly 10 is sequentially communicated, in the water inlet end of hyperfiltration membrane assembly 10 by described automatic
When rotating the connection of blow-off pipe 40, the delivery port 62 of its water side connection recoil automatic rotary plate 60.
Operation principle of the present utility model:Raw water enters in the inlet water tank 30 via the water inlet pipe 20, then distinguishes
Enter multiple hyperfiltration membrane assemblies 10 by multiple pipeline A80, multiple hyperfiltration membrane assemblies 10 were carried out to raw water
Filter is handled, and the production water of generation enters the water producing tank 50 by multiple pipeline B90 respectively, eventually passes the water producing pipe 70
Discharge.In whole filter process, the automatic rotation blow-off pipe 40 and the recoil automatic rotary plate 60 cooperate and carried out
Rotation, to realize in the backwash each other between multiple hyperfiltration membrane assemblies 10, the present embodiment, with the automatic rotation of the recoil
Disk 60 opens up exemplified by two water inlets 61 and a delivery port 62 to illustrate, specifically, when the recoil automatic rotary plate
60 rotate to two water inlets 61 and the delivery port 62 when being respectively communicated with three adjacent pipeline B90, it is described go out
The water inlet end of the hyperfiltration membrane assembly 10 that the mouth of a river 62 is connected just is connected by the automatic rotation blow-off pipe 40, and described in two
During the production water that two hyperfiltration membrane assemblies 10 that water inlet 61 is connected are produced can enter in the recoil automatic rotary plate 60
In empty cavity volume, then flow backwards and entered in the hyperfiltration membrane assembly 10 that is connected with the delivery port 62 by the delivery port 62, opened
Beginning is backwashed, and the sewage after backwash can be discharged via the automatic rotation blow-off pipe 40.Due to the delivery port 62
The water inlet end of the hyperfiltration membrane assembly 10 of connection is connected by the automatic rotation blow-off pipe 40, is somebody's turn to do so raw water will not also enter
Hyperfiltration membrane assembly 10, is smoothed out so as to ensure that to the backwash of the hyperfiltration membrane assembly 10.The recoil automatic rotary plate 60
It can continue to rotate under the active force of current, so as to backwash multiple hyperfiltration membrane assemblies 10 successively, whole process
Without shutdown processing.
Compared with prior art, the utility model can directly pass through without independently setting up backwash pipeline, valve, water pump
Automatic rotation blow-off pipe is used cooperatively with recoil automatic rotary plate, you can realize the recoil each other between each hyperfiltration membrane assembly
Wash, and avoid itself damaging for the film equipment that existing system running is caused due to continual stop and start device
Bad, the particularly fracture of wire problem of film silk realizes the continuous operation of system, greatly reduces overall investment and the system of film equipment
Complexity, while adding the service life of film.
Preferred embodiment of the present utility model is the foregoing is only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modification, equivalent substitution and improvements made etc. should be included in guarantor of the present utility model
Within the scope of shield.
Claims (7)
1. a kind of ultra-filtration membrane device continuously run without backwash pipeline, it is characterised in that including multiple hyperfiltration membrane assemblies, water inlet
Pipe, automatically inlet water tank, rotation blow-off pipe, water producing tank, recoil automatic rotary plate and water producing pipe, multiple hyperfiltration membrane assemblies are in ring
Shape is distributed, and the water inlet pipe connects the inlet water tank, and the inlet water tank connects multiple hyperfiltration membrane assemblies by multiple pipeline A
Water inlet end, the water producing tank connects multiple hyperfiltration membrane assembly water sides, the automatic rotation blow-off pipe by multiple pipeline B
It is arranged in the inlet water tank, the recoil automatic rotary plate is arranged in the water producing tank, and the water producing pipe connects the production
Water tank, the recoil automatic rotary plate is a hollow cavity, and two water inlets and a delivery port are at least offered above, described
Automatic rotation blow-off pipe is sequentially communicated each hyperfiltration membrane assembly water inlet end, the hyperfiltration membrane assembly water inlet end by it is described from
During dynamic rotation blow-off pipe connection, the delivery port of its water side connection recoil automatic rotary plate.
2. the ultra-filtration membrane device as claimed in claim 1 continuously run without backwash pipeline, it is characterised in that the pipeline A, institute
State pipeline B and the hyperfiltration membrane assembly three quantity is equal.
3. the as claimed in claim 1 ultra-filtration membrane device continuously run without backwash pipeline, it is characterised in that the inlet water tank and
The water producing tank is cylindric casing.
4. the ultra-filtration membrane device as claimed in claim 3 continuously run without backwash pipeline, it is characterised in that multiple pipelines
A is placed equidistant in the side of the inlet water tank, and multiple pipeline A and the inlet water tank tie point are located at same level
Face, multiple pipeline B are placed equidistant in the side of the water producing tank, and multiple pipeline B and the connection of the water producing tank
Point is located at same level.
5. the ultra-filtration membrane device as claimed in claim 4 continuously run without backwash pipeline, it is characterised in that the automatic rotation
Blow-off pipe is rotated around the axis of the inlet water tank, and the recoil automatic rotary plate is rotated around the axis of the water producing tank.
6. the ultra-filtration membrane device as claimed in claim 5 continuously run without backwash pipeline, it is characterised in that the recoil is automatic
Rotating disk is integrally curved, and its external diameter is equal to the internal diameter of the water producing tank.
7. the ultra-filtration membrane device as claimed in claim 6 continuously run without backwash pipeline, it is characterised in that the recoil is automatic
Camber line distance in rotating disk between the adjacent water inlet or the delivery port is equal to the two neighboring pipeline B and the production
Camber line distance between water tank tie point.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621478192.8U CN206372699U (en) | 2016-12-30 | 2016-12-30 | A kind of ultra-filtration membrane device continuously run without backwash pipeline |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621478192.8U CN206372699U (en) | 2016-12-30 | 2016-12-30 | A kind of ultra-filtration membrane device continuously run without backwash pipeline |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206372699U true CN206372699U (en) | 2017-08-04 |
Family
ID=59408465
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621478192.8U Active CN206372699U (en) | 2016-12-30 | 2016-12-30 | A kind of ultra-filtration membrane device continuously run without backwash pipeline |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206372699U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106731848A (en) * | 2016-12-30 | 2017-05-31 | 武汉艾科滤膜技术有限公司 | A kind of ultra-filtration membrane device continuously run without backwash pipeline |
GB2626429A (en) * | 2023-05-17 | 2024-07-24 | Univ Guilin Technology | Water purification device using gradient functional membrane with graphene-induced orientation |
-
2016
- 2016-12-30 CN CN201621478192.8U patent/CN206372699U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106731848A (en) * | 2016-12-30 | 2017-05-31 | 武汉艾科滤膜技术有限公司 | A kind of ultra-filtration membrane device continuously run without backwash pipeline |
GB2626429A (en) * | 2023-05-17 | 2024-07-24 | Univ Guilin Technology | Water purification device using gradient functional membrane with graphene-induced orientation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2023231277A1 (en) | Automatic backwashing filtration apparatus and method for low-temperature multi-effect distillation seawater desalination system | |
CN201231137Y (en) | Continuous filter device | |
CN206372699U (en) | A kind of ultra-filtration membrane device continuously run without backwash pipeline | |
CN104402094A (en) | Energy-saving and pollution-resisting water treatment system provided with RO (reverse osmosis) membranes and application of water treatment system | |
CN110514048B (en) | Cooling water saving process for circulating water pump of direct-current cooling water-heating power unit | |
CN106731848A (en) | A kind of ultra-filtration membrane device continuously run without backwash pipeline | |
CN201671609U (en) | Closed tank-free oilfield water injection system with controllable pressure and flow | |
CN103626311A (en) | Low-yield single-pump two-stage reverse osmosis system | |
CN205361072U (en) | Abluent reverse osmosis membrane system, does not shut down | |
CN104803516A (en) | Integrated container type sea water desalting equipment and desalting process thereof | |
CN101185847A (en) | Ceramic film backwash method | |
CN210905705U (en) | System special for reverse osmosis membrane test | |
CN204607721U (en) | Reverse osmosis water treating equipment | |
CN208611916U (en) | A kind of backpulsing water filtering device | |
CN207025096U (en) | Receive filter membrane device | |
CN203329484U (en) | Filter of household ultra-filtration water purifier | |
CN206631442U (en) | A kind of tubular membrane component of inwall coating | |
CN202506317U (en) | Reverse osmosis membrane pulse filter | |
CN210613387U (en) | Non-stop cleaning anti-pollution reverse osmosis membrane device | |
CN207079089U (en) | The improved RO systems that single putamina cleaning can be achieved | |
CN109529625A (en) | Continuous nanofiltration process for alkali liquor | |
CN110107545A (en) | A kind of pressure-exchange supercharger arrangement | |
CN205528200U (en) | Novel system pure water reverse osmosis system | |
CN111076503A (en) | Vacuum drying furnace device for hard alloy and drying method | |
CN204607722U (en) | Water treating equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |