CN207266828U - The membrane equipment of the reinforced ultrafiltration membrane of high throughput - Google Patents
The membrane equipment of the reinforced ultrafiltration membrane of high throughput Download PDFInfo
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- CN207266828U CN207266828U CN201721098417.1U CN201721098417U CN207266828U CN 207266828 U CN207266828 U CN 207266828U CN 201721098417 U CN201721098417 U CN 201721098417U CN 207266828 U CN207266828 U CN 207266828U
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- level
- membrane
- high throughput
- trailer
- reinforced
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- 239000012528 membrane Substances 0.000 title claims abstract description 35
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 230000001112 coagulating effect Effects 0.000 claims abstract description 32
- 238000002360 preparation method Methods 0.000 claims abstract description 31
- 238000002407 reforming Methods 0.000 claims abstract description 28
- 238000009987 spinning Methods 0.000 claims abstract description 24
- 238000001035 drying Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 18
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000004804 winding Methods 0.000 claims description 7
- 238000007711 solidification Methods 0.000 claims description 3
- 230000008023 solidification Effects 0.000 claims description 3
- 238000012805 post-processing Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 230000004048 modification Effects 0.000 abstract description 6
- 238000012986 modification Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 description 2
- 230000010148 water-pollination Effects 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000004506 ultrasonic cleaning Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of membrane equipment of the reinforced ultrafiltration membrane of high throughput, belongs to film forming apparatus technical field.Including adjacent successively at the uniform velocity paying off system, reforming system and drying system, the drying system, the first trailer system, spinning head are adjacent successively, the spinning head connection film liquid supplying device, spinning head, humiture path control system and fast pore-creating system are adjacent successively, the fast pore-creating system, level-one coagulating tank, two level coagulating tank are adjacent successively, the secondary cycle sink end connects the second trailer system, the second trailer system connection after-treatment system.The beneficial effects of the utility model are：Reinforced wire enhances the bonding force of film wire after modification, is modified by preparation liquid, passage, fast pore-creating, coagulating bath, online film wire, and equipment operation is simple, easy control of process conditions, and production efficiency is high.
Description
Technical field
A kind of membrane equipment of ultrafiltration membrane is the utility model is related to, belongs to film forming apparatus technical field.
Background technology
Traditional membrane equipment, the bonding force of film wire is small, and equipment operation is complicated, and film wire aperture is big and not easy to control, film
Silk one-tenth porosity is few, and film wire flux is low, and process conditions are difficult to control and low production efficiency.
Utility model content
To solve defect existing in the prior art, the purpose of this utility model is to provide a kind of reinforced ultrafiltration membrane of high throughput
Membrane equipment, by the special modification of reinforced wire, improve product quality, the equipment operation is simple, process conditions are easily controlled
System, production efficiency are high.
The technical solution of the utility model is：The membrane equipment of the reinforced ultrafiltration membrane of high throughput, including it is adjacent even successively
Fast paying off system, reforming system and drying system, the drying system, the first trailer system, spinning head are adjacent successively, described
Spinning head connection film liquid supplying device, spinning head, humiture path control system and fast pore-creating system are adjacent successively,
The fast pore-creating system, level-one coagulating tank, two level coagulating tank are adjacent successively, the level-one coagulating tank, two level solidification
Bath is respectively communicated with the primary cycle sink and secondary cycle sink of lower section, second traction of secondary cycle sink end connection
System, the second trailer system connection after-treatment system.
The reforming system includes reforming system a and reforming system b, and the reforming system a is filled by unwrapping wire Torque Control
Put connection reforming system b.
First trailer system is five roller trailer systems, and second trailer system is seven roller trailer systems, described five
The reinforced wire outlet of roller trailer system, spinning head humiture path control system and fast pore-creating system is in same level
On line.
The film liquid supplying device includes, preparation liquid reaction system, the preparation liquid reaction system connection preparation liquid storage
Tank is deposited, the preparation liquid holding vessel connects high-precision filter by preparation liquid delivery pump, and the high-precision filter passes through meter
Amount pump connection spinning head, the preparation liquid reaction system connect nitrogen by nitrogen pipeline respectively with preparation liquid holding vessel and input
System.
Unwrapping wire moment control device is equipped between the at the uniform velocity paying off system, reforming system and drying system.
The primary cycle sink passes through the both ends of the circulating water pipe a connections level-one coagulating tank, the circulating water pipe a
Primary cycle water pump is equipped with, the secondary cycle sink passes through the both ends of the circulating water pipe b connections two level coagulating tank, institute
State circulating water pipe b and be equipped with secondary cycle water pump.
The after-treatment system includes, the ultrasonic cleaner adjacent with the second trailer system, ultrasonic cleaner, ultrasound
Ripple rear treating groove, film wire automatic adjustment device, film wire winding wheel are adjacent successively, and the film wire winding wheel is located above sink.
Be respectively equipped with heating unit in the ultrasonic cleaner, ultrasonic wave rear treating groove, sink, heating-up temperature for 0~
80℃。
Heating unit is equipped with the level-one coagulating tank, two level coagulating tank, heating-up temperature is 0~80 DEG C.
The distance of humiture path control system and spinning head is 100-300mm, humiture path control system
It is 300-800mm with fast pore-creating system distance, the level-one coagulating tank is 200-500mm with fast pore-creating system distance.
The beneficial effects of the utility model are：Reinforced wire enhances the bonding force of film wire after modification, passes through system
Film liquid, passage, fast pore-creating, coagulating bath, online film wire are modified, and equipment operation is simple, easy control of process conditions, production efficiency
It is high.
Brief description of the drawings
Fig. 1 is the utility model structure diagram.
Reference numeral is as follows in figure：1st, at the uniform velocity paying off system, 2, unwrapping wire moment control device, 3, reforming system, 4, drying
System, the 5, first trailer system, 6, spinning head, 7, humiture path control system, 8, fast pore-creating system, 9, level-one solidification
Bath, 10, two level coagulating tank, 11, primary cycle sink, 12, secondary cycle sink, the 13, second trailer system, 14, level-one
Water circulating pump, 15, secondary cycle water pump, 16.1, preparation liquid reaction system, 16.2, preparation liquid holding vessel, 16.3, nitrogen input
System, 16.4, high-precision filter, 16.5, metering pump, 16.6, preparation liquid delivery pump, 17.1, ultrasonic cleaner, 17.2,
Ultrasonic wave rear treating groove, 17.3, film wire automatic adjustment device, 17.4, film wire winding wheel, 17.5, sink.
Embodiment
1 pair of the utility model is described further below in conjunction with the accompanying drawings：
The membrane equipment of the reinforced ultrafiltration membrane of high throughput, including at the uniform velocity paying off system 1 adjacent successively, 3 and of reforming system
Drying system 4, the drying system 4, the first trailer system 5, spinning head 6 are adjacent successively, the connection of spinning head 6 film
Liquid supplying device, spinning head 6, humiture path control system 7 and fast pore-creating system 8 are adjacent successively, the fast pore-creating
System 8, level-one coagulating tank 9, two level coagulating tank 10 are adjacent successively, and the level-one coagulating tank 9, two level coagulating tank 10 divide
Not Lian Tong lower section primary cycle sink 11 and secondary cycle sink 12, the second traction of 12 end of secondary cycle sink connection
System 13, the second trailer system 13 connection after-treatment system.The at the uniform velocity paying off system 1 is by controlling the velocity of rotation of draw drum
Realize uniform unwrapping wire；The drying system 4 controls heating-up temperature by electric boiling plate, modified reinforced wire is uniformly done rapidly
It is dry.For humiture path control system 7 by heating and temperature control device, the aqueous solvent for making to prepare is heated to 120 degree, forms water and steams
Gas and then enter one by pipeline and have in the container of nitrogen, temperature control in required scope, then this gaseous mixture
Body inputs path, and making to become inside path has the constant temperature and humidity space with solvent.The fast pore-creating system 8 includes closing
Liquid packing groove, the interior liquid being equipped with preparation liquid reaction of groove, after reaction, quickly solidifies on film wire surface and forms filtering
Hole, fluid temperature are controlled by constant temperature water tank.It is hydrophilic that film wire is equipped between the level-one coagulating tank 9 and two level coagulating tank 10
Reforming system, increases film wire hydrophily, so as to improve the water filtration efficiency of film wire.
The reforming system 3 includes reforming system a and reforming system b, and the reforming system a is filled by unwrapping wire Torque Control
Put 2 connection reforming system b.Reforming system a increases the adhesive effect of reinforced wire, beneficial to the attachment of preparation liquid；Reforming system b is acted on
It is the water flowing efficiency that film wire is improved to increase hydrophily.The power required when can be according to spinning of unwrapping wire moment control device 2
Square, is controlled draw drum.Reforming system 3 is reinforced wire is passed through from modification liquid, and enhancing reinforced wire is bonding with film liquid
Effect.Reforming system b and the distance of the spinning head 6 are 1200~2000mm.
First trailer system 5 is five roller trailer systems, and second trailer system 13 is seven roller trailer systems, described
The reinforced wire outlet of five roller trailer systems, 6 humiture path control system 7 of spinning head and fast pore-creating system 8 is in same
On one horizontal line.
The film liquid supplying device includes, and preparation liquid reaction system 16.1, the preparation liquid reaction system 16.1 connects
Preparation liquid holding vessel 16.2, the preparation liquid holding vessel 16.2 connect high-precision filter by preparation liquid delivery pump 16.3
16.4, the high-precision filter 16.4 connects spinning head 6,16.1 He of preparation liquid reaction system by metering pump 16.5
Preparation liquid holding vessel 16.2 connects nitrogen input system 16.3 by nitrogen pipeline respectively.Nitrogen input system 16.3 is used to control
The discharge pressure of preparation liquid, high-precision filter 16.4 filter fine impurities all in preparation liquid, and metering pump 16.5 is used to monitor
Into the speed of the preparation liquid of spinning head 6.
Unwrapping wire moment control device 2 is equipped between the at the uniform velocity paying off system 1, reforming system 3 and drying system 4.
The primary cycle sink 11 passes through the both ends of the circulating water pipe a connections level-one coagulating tank 9, the recirculated water
Pipe a is equipped with primary cycle water pump 14, and the secondary cycle sink 12 passes through the circulating water pipe b connections two level coagulating tank 10
Both ends, the circulating water pipe b is equipped with secondary cycle water pump 15.
The after-treatment system includes, the ultrasonic cleaner 17.1 adjacent with the second trailer system 13, ultrasonic cleaning
Groove 17.1, ultrasonic wave rear treating groove 17.2, film wire automatic adjustment device 17.3, film wire winding wheel 17.4 are adjacent successively, the film wire
Winding wheel 17.4 is located at the top of sink 17.5.
Heating unit is respectively equipped with the ultrasonic cleaner 17.1, ultrasonic wave rear treating groove 17.2, sink 17.5, is added
Hot temperature is 0~80 DEG C.Ultrasonic cleaner 17.1, ultrasonic wave rear treating groove 17.2 are respectively provided with the super of three pieces of different frequencies
Sound wave shock plate, its supersonic frequency are 30~50KHZ.
Heating unit is equipped with the level-one coagulating tank 9, two level coagulating tank 10, heating-up temperature is 0~80 DEG C.
Humiture path control system 7 and the distance of spinning head 6 are 100-300mm, and the control of humiture path is
System 7 and fast pore-creating system 8 are apart from for 300-800mm, and the level-one coagulating tank 9 and fast pore-creating system 8 are apart from for 200-
500mm。
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art
For art personnel, on the premise of the utility model technical principle is not departed from, some improvement and modification can also be made, these change
The scope of protection of the utility model is also should be regarded as into modification.
Claims (10)
1. a kind of membrane equipment of the reinforced ultrafiltration membrane of high throughput, it is characterised in that including at the uniform velocity paying off system adjacent successively
(1), reforming system (3) and drying system (4), the drying system (4), the first trailer system (5), spinning head (6) are successively
It is adjacent, the spinning head (6) connection film liquid supplying device, spinning head (6), humiture path control system (7) and soon
Rapid-result hole system (8) is adjacent successively, the fast pore-creating system (8), level-one coagulating tank (9), two level coagulating tank (10) according to
Secondary adjacent, the level-one coagulating tank (9), two level coagulating tank (10) are respectively communicated with the primary cycle sink (11) and two of lower section
Level circulating water chennel (12), secondary cycle sink (12) end connect the second trailer system (13), the second trailer system (13)
Connect after-treatment system.
2. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the reforming system
(3) include reforming system a and reforming system b, the reforming system a and reforming system is connected by unwrapping wire moment control device (2)
b。
3. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that first traction
System (5) is five roller trailer systems, and second trailer system (13) is seven roller trailer systems, and the five rollers trailer system, spin
The outlet of the reinforced wire of silk head (6) humiture path control system (7) and fast pore-creating system (8) is in same horizontal line
On.
4. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the preparation liquid supplies
Include to device, preparation liquid reaction system (16.1), the preparation liquid reaction system (16.1) connects preparation liquid holding vessel
(16.2), the preparation liquid holding vessel (16.2) connects high-precision filter (16.4), institute by preparation liquid delivery pump (16.6)
State high-precision filter (16.4) and spinning head (6), the preparation liquid reaction system (16.1) are connected by metering pump (16.5)
Nitrogen input system (16.3) is connected by nitrogen pipeline respectively with preparation liquid holding vessel (16.2).
5. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the at the uniform velocity unwrapping wire
Unwrapping wire moment control device (2) is equipped between system (1), reforming system (3) and drying system (4).
6. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the primary cycle
Sink (11) is followed by the both ends of the circulating water pipe a connections level-one coagulating tank (9), the circulating water pipe a equipped with level-one
Ring water pump (14), the secondary cycle sink (12) pass through the both ends of the circulating water pipe b connections two level coagulating tank (10), institute
State circulating water pipe b and be equipped with secondary cycle water pump (15).
7. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the post processing system
System includes, the ultrasonic cleaner (17.1) adjacent with the second trailer system (13), after ultrasonic cleaner (17.1), ultrasonic wave
Treatment trough (17.2), film wire automatic adjustment device (17.3), film wire winding wheel (17.4) are adjacent successively, the film wire winding wheel
(17.4) above sink (17.5).
8. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 7, it is characterised in that the ultrasonic wave is clear
Heating unit is respectively equipped with washing trough (17.1), ultrasonic wave rear treating groove (17.2), sink (17.5), heating-up temperature is 0~80
℃。
9. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the level-one solidification
Heating unit is equipped with bath (9), two level coagulating tank (10), heating-up temperature is 0~80 DEG C.
10. the membrane equipment of the reinforced ultrafiltration membrane of high throughput according to claim 1, it is characterised in that the humiture
Path control system (7) and the distance of spinning head (6) are 100-300mm, humiture path control system (7) and fast pore-creating
System (8) distance is 300-800mm, and the level-one coagulating tank (9) is 200-500mm with fast pore-creating system (8) distance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721098417.1U CN207266828U (en) | 2017-08-30 | 2017-08-30 | The membrane equipment of the reinforced ultrafiltration membrane of high throughput |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721098417.1U CN207266828U (en) | 2017-08-30 | 2017-08-30 | The membrane equipment of the reinforced ultrafiltration membrane of high throughput |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207266828U true CN207266828U (en) | 2018-04-24 |
Family
ID=61960111
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721098417.1U Active CN207266828U (en) | 2017-08-30 | 2017-08-30 | The membrane equipment of the reinforced ultrafiltration membrane of high throughput |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207266828U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107376649A (en) * | 2017-08-30 | 2017-11-24 | 碧菲分离膜（大连）有限公司 | The membrane equipment of the reinforced milipore filter of high flux |
-
2017
- 2017-08-30 CN CN201721098417.1U patent/CN207266828U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107376649A (en) * | 2017-08-30 | 2017-11-24 | 碧菲分离膜（大连）有限公司 | The membrane equipment of the reinforced milipore filter of high flux |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Membrane making equipment for high-throughput enhanced ultrafiltration membranes Effective date of registration: 20231204 Granted publication date: 20180424 Pledgee: Bank of China Limited Dalian Jinpu New Area Branch Pledgor: BIFEI SEPARATION MEMBRANE (DALIAN) CO.,LTD. Registration number: Y2023980069158 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |