CN209519610U - A kind of ultrafiltration membrane material filtering system - Google Patents
A kind of ultrafiltration membrane material filtering system Download PDFInfo
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- CN209519610U CN209519610U CN201920117647.0U CN201920117647U CN209519610U CN 209519610 U CN209519610 U CN 209519610U CN 201920117647 U CN201920117647 U CN 201920117647U CN 209519610 U CN209519610 U CN 209519610U
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- ultrafiltration membrane
- filter mechanism
- filter
- purge tank
- level filter
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Abstract
The utility model innovation provides a kind of ultrafiltration membrane material filtering system of high efficiency circulating filtration.This kind of ultrafiltration membrane material filtering system, including feeding device, filter device, cooling device and cleaning device, the feeding device include material pot and by connecting tube and the tank connected charging pump of material；The filter device includes the first level filter mechanism and the second level filter mechanism, and the first level filter mechanism is made of multiple groups cartridge filter, and the second level filter mechanism is made of multiple groups membrane tube, and the hollow-fibre membrane in the membrane tube is ultrafiltration membrane；The cooling device includes the cooling tube of heat exchanger and connection on heat exchangers, and the cleaning device includes purge tank and the heating mechanism inside purge tank.This ultrafiltration membrane material filtering system carries out double filtration using multiple groups cartridge filter and multiple groups ultrafiltration membrane pipe, and multiple groups cartridge filter can filter out the macromolecular particle in material, such as sand, stone, avoids the filter hole of macromolecular particle blocking ultrafiltration membrane；Cooling device flows through heat exchanger by cooling water to realize cooling.
Description
Technical field
The utility model belongs to material filtering field more particularly to a kind of ultrafiltration membrane material filtering system.
Background technique
Ultrafiltration membrane material filtering system is a kind of system being filtered by ultrafiltration membrane pipe, existing ultrafiltration membrance filter system
System is all the relatively simple material for filtering needs by ultrafiltration membrane pipe, will treat as final filtration by the material of ultrafiltration membrane pipe
Good material, and for the material higher to some solid contents in this way, viscosity is larger, solid particle is more, due to ultrafiltration membrane pipe
Channel diameter is smaller, and channel blockage may be influenced the service efficiency of film by these materials；According to the property of material, need to formulate not
It is synthermal, and existing system can not achieve recycling.
Summary of the invention
In view of the shortcomings of the prior art, the utility model innovation provides a kind of ultrafiltration membrane of high efficiency circulating filtration
Material filtering system.
This kind of ultrafiltration membrane material filtering system, including feeding device, filter device, cooling device and cleaning device, institute
It states feeding device, filter device and cooling device to connect by connecting tube, the cleaning device is connected in parallel on by connecting tube to be added
Expect on device, the feeding device includes material pot and by connecting tube and the tank connected charging pump of material；The filtering dress
It sets including the first level filter mechanism and the second level filter mechanism, the first level filter mechanism is by multiple groups cartridge filter
Composition, the second level filter mechanism are made of multiple groups membrane tube, and the hollow-fibre membrane in the membrane tube is ultrafiltration membrane；It is described cold
But device includes the cooling tube of heat exchanger and connection on heat exchangers, and the cooling device is arranged in the first level filter mechanism
And second between level filter mechanism；The cleaning device includes purge tank and the heating mechanism inside purge tank, institute
The Matter Transfer mouth for being equipped at the top of material pot and connecting with the second level filter mechanism is stated, the purge tank top is equipped with and the second layer
The water circulation port of secondary filter mechanism connection.
The heat exchanger upper end is parallel with a straight-through connecting tube, leads directly to connecting tube and is equipped with control valve, the cooling dress
It sets and is equipped with instruction disk between the second level filter mechanism.
Described second level filter mechanism one end is equipped with drainage pipeline.
Water filling port is equipped at the top of the material pot.
Water filling port is equipped at the top of the purge tank, the heating mechanism inside the purge tank is made of jet chimney, described
Jet chimney is arranged in a curve way inside purge tank, and the air inlet and air outlet of jet chimney are arranged at outside purge tank.
According to ultrafiltration membrane material filtering system provided by the utility model, using multiple groups cartridge filter and multiple groups ultrafiltration membrane
Pipe carries out double filtration, and multiple groups cartridge filter can filter out the macromolecular particle in material, such as sand, stone, avoids dividing greatly
The filter hole of sub- particle blocking ultrafiltration membrane；Cooling device flows through heat exchanger by cooling water to realize cooling, and cleaning device can be right
The connecting tube and filter device of whole system are cleaned, and the recyclable cleaning of the water in cleaning device, until clear water becomes dirty
After water, it is discharged therewith.
Detailed description of the invention
Fig. 1 is the overall flow structure chart of the utility model.
Specific embodiment
As shown in Figure 1, this ultrafiltration membrane material filtering system, including feeding device, filter device, cooling device and clear
Cleaning device, and feeding device, filter device and cooling device are connected by connecting tube, cleaning device is connected in parallel on by connecting tube
On feeding device, it is filtered to make the material in material pot 1 flow to subsequent device out of tank, feeding device includes material
Tank 1 and the charging pump 2 being connect by connecting tube with material pot 1；In order to avoid the macromolecular particle in material blocks ultrafiltration membrane
Filter hole, filter device include the first level filter mechanism 3 and the second level filter mechanism 4, due to 31 energy of cartridge filter
Large particulate matter is filtered out, the effect of primary filtration is also able to achieve, is filtered so the first level filter mechanism 3 is ensured public security by multiple groups
Device 31 forms, and due to needing to carry out deeper filtering to material, filters out the pure substance needed in material, so by the
Two level filter mechanisms 4 are made of multiple groups membrane tube 41, and the hollow-fibre membrane in membrane tube 41 is ultrafiltration membrane, and the aperture of ultrafiltration membrane exists
0.01 micron hereinafter, the spot in material greater than 0.01 micron or more can be filtered out；Due to the material initial temperature in material pot 1
It is just relatively high, material flow direction filtering at a high speed under the action of passing through charging pump 2 generally in 60 DEG C -70 DEG C, material pot 1
In device, the flow at high speed of material can be such that temperature of charge increases, and the material at this moment needing to heat up is cooled down, and most simple saving
The type of cooling be to be cooled down by cold water, cooling device includes heat exchanger 5 and the cooling tube being connected on heat exchanger 56, cold
Water constantly flows in cooling tube 6, plays cooling effect, and cooling device is arranged in the first level filter mechanism 3 and second
Between level filter mechanism 4, since material is not having power to continue to flow in the second level filter mechanism 4 after heat exchanger 5；
Since the cleaning effect of hot water is higher than the cleaning effect of cold water, cleaning device includes purge tank 8 and is located inside purge tank 8
Heating mechanism the object connecting with the second level filter mechanism 4 is equipped at the top of material pot 1 since material filtering can have a residue
Expect circulation port 12, remaining material will be flowed into material pot 1 by connecting tube and Matter Transfer mouth 12, for mistake next time
Filter, since the hot water in purge tank 8 is in cleaning system pipeline and device, first pass punching is not washed clean, and needs circulation flushing, institute
To be equipped with the water circulation port 10 connecting with the second level filter mechanism 4 at the top of purge tank 8, hot water passes through after rinsing first pass
Connecting tube and water circulation port 10 flow into purge tank 8, clean for second.
5 upper end of heat exchanger in the utility model is parallel with a straight-through connecting tube 7, leads directly to connecting tube 7 and is equipped with control
Valve 71 is equipped with instruction disk 72 between cooling device and the second level filter mechanism 4, since material is being subjected to the former pressure of charging pump 2
It quickly circulates after power, the material in material pot 1 will flow in cooling device at a high speed, and at this moment the flow of material is excessive, and material needs
It is flowed in the second level filter mechanism 4 by straight-through connecting tube 7, control valve 71 flows through straight-through connecting tube 7 for material is automatically controlled.
4 one end of the second level filter mechanism in the utility model is equipped with drainage pipeline 9, due to the hot water in purge tank 8
After cleaning end conduit and device, clear water will become sewage, and sewage can be discharged by drainage pipeline 9.
Water filling port 11 is equipped at the top of material pot 1 in the utility model, when material needs one in carrying out subsequent filtering
Fixed pure water is mixed, so being equipped with the opening of an addition pure water at the top of material pot 1.
Water filling port 11 is equipped at the top of purge tank 8 in the utility model, the heating mechanism inside purge tank 8 is by jet chimney
81 are constituted, and jet chimney 81 is arranged in a curve way inside purge tank 1, and the air inlet and air outlet of jet chimney 81 are arranged at cleaning
Outside tank 8, since heating effect of the steam to water is preferable, so the heating method of water is heated using steam in purge tank 8, steam
The bending setting of pipeline 81, steam input tank is interior bigger with the contact surface of water, and the time is longer, and heating effect is higher.
Claims (5)
1. a kind of ultrafiltration membrane material filtering system, including feeding device, filter device, cooling device and cleaning device, described
Feeding device, filter device and cooling device are connected by connecting tube, and the cleaning device is connected in parallel on charging by connecting tube
On device, it is characterised in that: the confession that the feeding device includes material pot (1) and connect with material pot (1) by connecting tube
Material pump (2)；The filter device includes the first level filter mechanism (3) and the second level filter mechanism (4), first level
Filter mechanism (3) is made of multiple groups cartridge filter (31), and the second level filter mechanism (4) is by multiple groups membrane tube (41) group
At the hollow-fibre membrane in the membrane tube (41) is ultrafiltration membrane；The cooling device includes heat exchanger (5) and is connected to heat exchange
Cooling tube (6) on device (5), the cooling device are arranged in the first level filter mechanism (3) and the second level filter mechanism (4)
Between；The cleaning device includes purge tank (8) and is located at purge tank (8) internal heating mechanism, and the material pot (1) is pushed up
Portion is equipped with the Matter Transfer mouth (12) connecting with the second level filter mechanism (4), and purge tank (8) top is equipped with and the second layer
The water circulation port (10) of secondary filter mechanism connection.
2. a kind of ultrafiltration membrane material filtering system according to claim 1, it is characterised in that: heat exchanger (5) upper end is simultaneously
It is associated with a straight-through connecting tube (7), connecting tube (7) is led directly to and is equipped with control valve (71), the cooling device and the second level mistake
Instruction disk (72) is equipped between filter structure (4).
3. a kind of ultrafiltration membrane material filtering system according to claim 1, it is characterised in that: the second level filter mechanism
(4) one end is equipped with drainage pipeline (9).
4. a kind of ultrafiltration membrane material filtering system according to claim 1, it is characterised in that: set at the top of the material pot (1)
There are water filling port (11).
5. a kind of ultrafiltration membrane material filtering system according to claim 1, it is characterised in that: set at the top of the purge tank (8)
Have water filling port (11), the internal heating mechanism of the purge tank (8) is made of jet chimney (81), and the jet chimney (81) is curved
Song setting is internal in purge tank (8), and it is external that the air inlet and air outlet of jet chimney (81) are arranged at purge tank (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920117647.0U CN209519610U (en) | 2019-01-24 | 2019-01-24 | A kind of ultrafiltration membrane material filtering system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920117647.0U CN209519610U (en) | 2019-01-24 | 2019-01-24 | A kind of ultrafiltration membrane material filtering system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209519610U true CN209519610U (en) | 2019-10-22 |
Family
ID=68230663
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920117647.0U Expired - Fee Related CN209519610U (en) | 2019-01-24 | 2019-01-24 | A kind of ultrafiltration membrane material filtering system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209519610U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116850786A (en) * | 2023-08-30 | 2023-10-10 | 开平牵牛生化制药有限公司 | Ultrafiltration membrane separation equipment with quick back flush function |
-
2019
- 2019-01-24 CN CN201920117647.0U patent/CN209519610U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116850786A (en) * | 2023-08-30 | 2023-10-10 | 开平牵牛生化制药有限公司 | Ultrafiltration membrane separation equipment with quick back flush function |
| CN116850786B (en) * | 2023-08-30 | 2023-11-07 | 开平牵牛生化制药有限公司 | Ultrafiltration membrane separation equipment with quick back flush function |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191022 Termination date: 20220124 |