CN207591634U - Interface moves dock cellulosic ultrafiltration putamina - Google Patents
Interface moves dock cellulosic ultrafiltration putamina Download PDFInfo
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- CN207591634U CN207591634U CN201721420180.4U CN201721420180U CN207591634U CN 207591634 U CN207591634 U CN 207591634U CN 201721420180 U CN201721420180 U CN 201721420180U CN 207591634 U CN207591634 U CN 207591634U
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- putamina
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- end cap
- ultrafiltration
- cellulosic ultrafiltration
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Abstract
A kind of interface moves dock cellulosic ultrafiltration putamina, including：Ultrafiltration membrane putamina ontology, is used to accommodate hollow-fibre membrane；It is arranged on the end cap of the putamina body end；The slider of liquid entrance is provided with, the slider is slidably connected on the end cap, and the relative position between liquid-inlet and outlet can be adjusted by the slip of above-mentioned slider；The liquid entrance refers to flow in or out the channel of the putamina body interior for liquid.The ultrafiltration putamina can be adapted to different ultrafiltration apparatus.
Description
Technical field
The utility model is related to technical field of membrane separation, and in particular to a kind of fiber filter putamina, more particularly to one kind
Interface moves dock cellulosic ultrafiltration putamina.
Background technology
Ultrafiltration is a kind of membrane separation technique, and solution purification can be detached or be concentrated.Ultrafiltration is with receiving between micro-filtration
Between filter, and without apparent line of demarcation between three.In general, the aperture of ultrafiltration membrane is between 0.05um -1nm, operation pressure
Power is 0.1-0.5Mpa.It is mainly used for the macromolecular substances such as suspended matter, colloid, particle, bacterium and virus that retention is gone in water removal.
The effect of ultrafiltration membrane is very extensive.Since it has separation, concentration, the characteristic of purifying biological product is flexibly employed for surpassing
The fields such as apparatus and blood treatment and wastewater treatment at the terminal of pure water.With increasingly improving for technology, ultrafiltration membrane
Filtering function has obtained greatly being promoted.To today, the industry for being related to filter plant is substantially all and can use.Such as
Separation of bacterial, heat source, colloid, suspended impurity and larger molecular organics are used in industrial water；Pure water is used in drinking water
The terminal processes prepared with ultra-pure water；It is used to detach drinking water, mineral spring Water warfare in industrial water；Fermentation, Enzymes Industry, system
Concentration, purifying and the clarification of medicine industry；Concentration of juices, separation；Point of soybean, dairy products, sugar industry, drinks, tea juice, vinegar etc.
From, concentration and clarification；The purification and recycling of industrial wastewater and sanitary sewage；The industries such as the recycling of electrophoretic paint.Hyperfiltration technique market
It is very huge.
In recent years, hyperfiltration technique is widely used in water treatment field due to having the characteristics that：
1. ultra-filtration process is to carry out at normal temperatures, mild condition is thus particularly suitable to thermo-responsive object without component damage
Matter, such as separation, classification, concentration and the enrichment of drug, enzyme, fruit juice.
2. ultrafiltration journey not undergoing phase transition, without heating, low energy consumption, pollution-free without adding chemical reagent, is a kind of section
The isolation technics of energy environmental protection.
3. hyperfiltration technique separative efficiency is high, the concentration of recycling, low concentration solution to the micro constitutent in weak solution is non-
Chang Youxiao.
4. ultra-filtration process is only with power of the pressure as UF membrane, therefore separator is simple, flow is short, operation is simple
Just, easily controllable and maintenance.
However, due to ultrafiltration membrane elements gradual aging in the process of running, water quality might have in various degree during operation
Variation, membrane component cleans by multiple chemical, can cause some expendable damages, flux reduction occur, ultrafiltration production water
Unqualified, the problems such as fracture of wire, performance cannot ensure.So ultrafiltration apparatus operation 3 to 5 years after, for ensure equipment it is normal
Operation, needs replacing membrane module.The variation of raw water quality proposes ultrafiltration membrane different requirements, continuous with masking technique
Progress, selected film brand is very likely different from the brand of early period during replacement.But the film size model number of each producer, water inlet
The differences such as mouth water outlet position cause to replace difficulty increase.
It can be seen that, it is necessary to study it is a kind of can be adapted to different manufacturers, different model has different water inlets and to go out
The ultrafiltration membrane shell of the ultrafiltration apparatus of mouth of a river position.
Utility model content
The purpose of this utility model is that propose a kind of ultrafiltration putamina that can be adapted to different ultrafiltration apparatus.
For this purpose, the utility model uses following technical scheme：
A kind of interface moves dock cellulosic ultrafiltration putamina, including：Ultrafiltration membrane putamina ontology is used to accommodate hollow fibre
Tie up film；It is arranged on the end cap of the putamina body end；The slider of liquid entrance is provided with, the slider is with slidably
Mode be connected on the end cap, by the slip of above-mentioned slider can adjust liquid-inlet and outlet between opposite position
It puts；The liquid entrance refers to flow in or out the channel of the putamina body interior for liquid.
As a preferred embodiment, end cap sliding rail is provided on end cap, slider track is provided on slider,
The sliding relative movement between end cap and slider is realized by the mutual cooperation of above-mentioned two track.
As a preferred embodiment, the end cap includes being separately positioned on upper end cover and the lower end at the putamina ontology both ends
It covers, correspondingly the slider includes upper end cover slider and bottom end cover slider.
As a preferred embodiment, the formwork ontology is cylinder, using UPVC materials, length 1500-2400mm, internal diameter
150-250mm。
As a preferred embodiment, the end cap be UPVC materials, length 200mm-400mm, internal diameter 160mm-250mm.
As a preferred embodiment, there are long 200mm-250mm, the hollow space of wide 50-70mm, hollow space on the end cap
There are sliding rail in both sides.
As a preferred embodiment, the leaf length of sliding is 300mm, width 55-75mm, and slip rail is connected on slider
Road can be connect with end cap.
As a preferred embodiment, after the relative position between liquid-inlet and outlet is regulated, be adhesively fixed the end
Lid and slider.
As a preferred embodiment, end cap is connected with putamina ontology using the either type in screw thread, buckle, bonding, welding.
As a preferred embodiment, opposite free sliding degree is multiple to the slider with the end cap.
The beneficial effects of the utility model are：By that (can be respectively upper in end cap to ultrafiltration membrane putamina appearance improvement
Lower cover) setting slider, the relative position relation of liquid entrance adjusted by the change of slider position, can with before
System slitless connection replaces the ultrafiltration membrane used early period, greatly reduces engineering cost, improve economic benefit.Such as upper and lower side
Lid using uniform structure, upper and lower end cap can phase double replacement use, installation is simple and practical, easy to operate.
Description of the drawings
Fig. 1 moves dock cellulosic ultrafiltration membrane shell structure schematic diagram for interface described in the utility model；
Fig. 2 is the slider structure diagram including liquid entrance of the ultrafiltration membrane membrane shell structure；
Fig. 3 is the sliding rail structure diagram of end cap up and down that the ultrafiltration membrane membrane shell structure includes.
Specific embodiment
Further illustrate the technical solution of the utility model below with reference to the accompanying drawings and specific embodiments.Here it needs
What is illustrated is attached drawing listed by the utility model merely to describing the problem the example arrangement signal that conveniently, provides
Figure, be a variety of achievable the utility model aim embodiment in one of them or several preferred embodiments, must not
It is correctly uniquely embodiment to be not understood as the utility model, must not more be not understood as the uniqueness limit to the utility model
System.
Fig. 1 is that interface described in the utility model moves dock cellulosic ultrafiltration putamina, and the cellulosic ultrafiltration putamina can
Think hollow fiber ultrafiltration putamina, including：Ultrafiltration membrane putamina ontology 1, for accommodating hollow-fibre membrane；Upper end cover 2, bottom end cover 3,
The end cap 2 and 3 up and down is arranged on the both ends of ultrafiltration membrane putamina ontology 1, is equipped with slider 6 on upper end cover 2, it is described on
End cap 2 is slidably connected with upper slider 6, and downslide movable plate 7 is equipped on bottom end cover 3, and the bottom end cover 3 is slided with downslide movable plate 7
Dynamic connection, above-mentioned be slidably connected may be used the structure of track cooperation and be achieved, and the degree of freedom of above-mentioned slip is not limited to one
On a direction, multivariant slide construction can be designed as needed；Such as：Above-mentioned slip can be along the putamina sheet
The slip in the central axial direction (longitudinal direction) of body 1；Above-mentioned slip can also be the central shaft around the putamina ontology 1 with rotation
Turn the slip of the relative motion of mode.
As a preferred embodiment, slide construction can be realized in the following way：Track 4 is set on upper end cover 2, in cunning
Track 8 is set on movable plate 6, and being cooperated by track 4 and track 8, it is relatively sliding between upper end cover 2 and upper slider 6 to realize
It is dynamic；Track 5 on bottom end cover 3 is set, track 9 is set on downslide movable plate 7, is cooperated by track 5 and track 9 under realizing
Opposite slip between end cap 3 and downslide movable plate 7.
Be respectively arranged with liquid entrance on slider 6 and downslide movable plate 7 on described, for separation to be filtered liquid into
Go out, aforesaid liquid is imported and exported with being connected inside the ultrafiltration membrane putamina.
By the mutual slip of above-mentioned upper slider 6 and downslide movable plate 7, the phase between aforesaid liquid inlet and outlet can be adjusted
To position, so as to dock with pipeline original in different system, with solve different manufacturers, different model with different water inlets and
The adaptation issues of ultrafiltration membrane shell when replacing ultrafiltration membrane of the ultrafiltration apparatus of water outlet position.
The putamina body part is UPVC materials, and shape is cylinder.
The length of putamina ontology 1 is 1500mm-2400mm, internal diameter 150mm-250mm.Preferred length 1860mm-2000mm,
Internal diameter 216mm.
The material of the upper end cover 2 and bottom end cover 3 is UPVC.Upper and lower side cover length 200mm-400mm, internal diameter 160mm-
250mm is connect, preferably end cap length 280mm-320mm, internal diameter 220mm-230mm with cylindrical putamina ontology 1.
There are long 200mm-250mm, the hollow space of wide 50mm-70mm on end cap, there are sliding rail in hollow space both sides.
The upper end cover is consistent with bottom end cover structure in some preferred embodiments, in order to be used interchangeably.
Preferably, the sliding rail 4 a length of 200mm-400mm, width 1mm-3mm on upper end cover 2.It is preferred that 280mm-
320mm, wide 2mm.Sliding rail 5 a length of 200mm-400mm, width 1mm-3mm on bottom end cover 3.It is preferred that 280mm-320mm,
Wide 2mm.
Preferably, upper 6 a length of 297mm-303mm of slider, width 50mm-80mm.Preferred length 300mm, wide 55mm-
75mm.Downslide movable plate 7 a length of 297mm-303mm, width 50mm-80mm.Preferred length 300mm wide 55mm-75mm.
Preferably, there is sliding rail 8 on upper slider 6, there is sliding rail 9 on downslide movable plate 7.Sliding rail 8 is a length of
200mm-400mm, width 1mm-3mm.It is preferred that 280mm-320mm, wide 2mm.9 a length of 200mm-400mm of sliding rail, width are
1mm-3mm.It is preferred that 280mm-320mm, wide 2mm.
Preferably, slider can be replaced arbitrarily.
Preferably, after liquid entrance relative position regulates, the fixed end cap and slider, it is preferable that above-mentioned
Fixation can be realized by way of bonding.
Upper end cover, bottom end cover and putamina ontology are connected using the either type in screw thread, buckle, bonding, welding.
It is understood that using the utility model, by the adjusting of slider position, change between liquid entrance
Distance, so as to being docked with pipeline original in different system, improve the substitutability of film.The slitless connection of ultrafiltration membrane, significantly
Engineering cost is reduced, improves economic benefit.Upper and lower end cover structure is consistent, can phase double replacement, simple and practical, operation side is installed
Just.
Embodiment 1
Hollow fiber film thread is seated in ultrafiltration putamina, sealing.Upper end cover with sliding rail is bonded in ultrafiltration
On film formwork, then the bottom end cover with sliding rail connect with putamina.Slider with track is installed to end cap up and down
Hollow space so that the spacing of upper and lower liquid entrance is 2150mm.The slider is bonded and fixed to end cap up and down.
Embodiment 2：
Hollow fiber film thread is seated in ultrafiltration putamina, sealing.Upper end cover with sliding rail is bonded in ultrafiltration
On film putamina, then the bottom end cover with sliding rail connect with putamina.Slider with track is installed to end cap up and down
Hollow space so that the spacing of upper and lower liquid entrance is 2110mm.The slider is bonded and fixed to end cap up and down.
The beneficial effects of the utility model are：By to ultrafiltration membrane putamina appearance improvement, being set respectively in upper and lower end cap
Slider adjusts the distance of liquid entrance by the change of slider position, can be replaced in system slitless connection before
The ultrafiltration membrane used early period, greatly reduces engineering cost, improves economic benefit.Upper and lower end cover structure is consistent, can mutually put
It changes, installation is simple and practical, easy to operate.
Although exemplary embodiment describing the utility model with reference to several, it is to be understood that, term used is explanation
With term exemplary, and not restrictive.Since the utility model can be embodied in a variety of forms without departing from practical new
The spirit or essence of type, it should therefore be appreciated that above-described embodiment is not limited to any aforementioned details, and should be in appended claims
It is widely explained in the spirit and scope limited, therefore falls into whole variations in claim or its equivalent scope and remodeling
Appended claims are all should be to be covered.
Claims (10)
1. a kind of interface moves dock cellulosic ultrafiltration putamina, it is characterized in that：Including：Ultrafiltration membrane putamina ontology, is used to hold
Receive hollow-fibre membrane；It is arranged on the end cap of the putamina body end；It is provided with the slider of liquid entrance, the slider
It is slidably connected on the end cap, can be adjusted between liquid-inlet and outlet by the slip of above-mentioned slider
Relative position；The liquid entrance refers to flow in or out the channel of the putamina body interior for liquid.
2. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：End cap sliding rail is provided on end cap, in cunning
Slider track is provided on movable plate, realizes that opposite slide between end cap and slider is transported by the mutual cooperation of two tracks
It is dynamic.
3. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The end cap includes being separately positioned on the putamina sheet
The upper end cover and bottom end cover at body both ends, correspondingly the slider include upper end cover slider and bottom end cover slider.
4. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The putamina ontology is cylinder, using UPVC materials
Matter, length 1500mm-2400mm, internal diameter 150-250mm.
5. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The end cap be UPVC materials, length 200mm-
400mm, internal diameter 160mm-250mm.
6. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：There is long 200mm-250mm on the end cap, it is wide
The hollow space of 50mm-70mm, hollow space both sides are provided with sliding rail.
7. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The slip leaf length is 300mm, width 55mm-
75mm is connected to sliding rail on slider, can be connect with end cap.
8. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：Adjusting the phase between determining liquid-inlet and exporting
Contraposition postpones, and be adhesively fixed the end cap and slider.
9. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The end cap and putamina ontology using screw thread, buckle,
Either type connection in bonding, welding.
10. cellulosic ultrafiltration putamina as described in claim 1, it is characterized in that：The slider opposite slip with the end cap
Degree of freedom is multiple.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721420180.4U CN207591634U (en) | 2017-10-30 | 2017-10-30 | Interface moves dock cellulosic ultrafiltration putamina |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721420180.4U CN207591634U (en) | 2017-10-30 | 2017-10-30 | Interface moves dock cellulosic ultrafiltration putamina |
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| Publication Number | Publication Date |
|---|---|
| CN207591634U true CN207591634U (en) | 2018-07-10 |
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ID=62757593
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721420180.4U Active CN207591634U (en) | 2017-10-30 | 2017-10-30 | Interface moves dock cellulosic ultrafiltration putamina |
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| Country | Link |
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| CN (1) | CN207591634U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107570013A (en) * | 2017-10-30 | 2018-01-12 | 安徽启迪清源新材料有限公司 | Interface may move dock cellulosic ultrafiltration putamina |
| CN111003753A (en) * | 2019-12-27 | 2020-04-14 | 苏州君康医疗科技有限公司 | Ultrafiltration device for preparing injection water and use method thereof |
-
2017
- 2017-10-30 CN CN201721420180.4U patent/CN207591634U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107570013A (en) * | 2017-10-30 | 2018-01-12 | 安徽启迪清源新材料有限公司 | Interface may move dock cellulosic ultrafiltration putamina |
| CN111003753A (en) * | 2019-12-27 | 2020-04-14 | 苏州君康医疗科技有限公司 | Ultrafiltration device for preparing injection water and use method thereof |
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