CN206467005U - A kind of multi-section serial ion-exchange fibre device - Google Patents
A kind of multi-section serial ion-exchange fibre device Download PDFInfo
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- CN206467005U CN206467005U CN201720096046.7U CN201720096046U CN206467005U CN 206467005 U CN206467005 U CN 206467005U CN 201720096046 U CN201720096046 U CN 201720096046U CN 206467005 U CN206467005 U CN 206467005U
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- Prior art keywords
- cylinder
- ion
- support tube
- central support
- exchange
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- 239000000835 fiber Substances 0.000 title claims abstract description 47
- 238000005342 ion exchange Methods 0.000 title claims abstract description 36
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 5
- 238000001914 filtration Methods 0.000 claims abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 6
- 239000011148 porous material Substances 0.000 claims description 6
- 230000008929 regeneration Effects 0.000 claims description 4
- 238000011069 regeneration method Methods 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 150000002500 ions Chemical class 0.000 description 9
- 238000007789 sealing Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 3
- 238000011049 filling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model is related to a kind of multi-section serial ion-exchange fibre device, it is used as agent structure using pillar cylinder and central support tube with certain bearing capacity, central support tube two ends are blocked with pipe plug, ion-exchange fibre is filled between the cylinder and central support tube, layering is separated by subregion filter plate between the cylinder and the central support tube, the ion-exchange fibre carries out multi-section serial with this, and every layer of subregion filter plate is fixed between the central support tube and the cylinder.It is big that this structure of the present utility model effectively improves ion fiber filtration resistance, the situation of operational effect difference, increase discharge capacity simultaneously, so that using ion exchange technique, using big flow, the method for operation of skinny device is achieved, and is solved in the past big using ion exchange pot floor space, the problem of flow is small, reduces operating cost.
Description
Technical field
The utility model is related to a kind of water treatment facilities, more particularly to a kind of multi-section serial ion-exchange fibre device, category
In technical field of water treatment equipment.
Background technology
Ion-exchange fibre is a kind of fibrous ion exchange material, when it is with electrolyte solution contacts, on fiber from
Son can make with the ion in solution it is selective exchange, be divided into cation exchange fibre, anion-exchange fibre and both sexes from
Sub- exchange fiber.It is widely used in desalinization, the preparation of industrial soft water, the production without ion pure water and salt industry.From
Sub- exchange fiber is as new functional macromolecule material, the superior performance compared with ion exchange resin, big with specific surface area, from
Sub- exchange velocity is fast, the characteristics of easily regenerating, and is easy to be loaded on various points with the different-thickness such as fibre bundle, netted, film and form
From in equipment.Therefore spherical, powdery macroreticular resin gradually a times fibrous separation material will be substituted, and be current separation and Extraction point
One of direction from Technical Research Center.
At present, in water treatment field, ion exchange is carried out generally in ion-exchanger, the similar pressure filter of ion-exchanger
Pond, shell is a cylinder of steel；Ion exchange generally uses filter type, and filter bed is made up of exchanger.And using ion fiber as filling
During thing, anti-current-rush ability is weaker, once fibrous layer will certainly be caused to be compacted as filter bed by the way of integrally filling,
Resistance to water-flow is increased, and can not only be given full play to ion fiber and be had the advantage that, while increasing system energy consumption, the regeneration of fiber
It is frequent with maintenance work.Therefore, ion exchange work directly should not be carried out using overall type of feed.
Utility model content
Deficiency and missing of the utility model for existing ion-exchange fibre equipment, it is proposed that a kind of novel multiple section series connection
Ion-exchange fibre device, i.e., it is internal using pillar cylinder and central support tube with certain bearing capacity as agent structure
Ion-exchange fibre is filled, and ion fiber is subjected to multilayer series connection, so as to realize ion-exchange fibre processing brackish water, big
Stable operation under flow, reduces the purpose of equipment overall cost.
The technical solution of the utility model is：
A kind of multi-section serial ion-exchange fibre device, it is with pillar cylinder and central supported with certain bearing capacity
Pipe is blocked as agent structure, central support tube two ends with pipe plug, is handed between the cylinder and central support tube filled with ion
Change fiber, it is characterised in that layering is separated by subregion filter plate between the cylinder and the central support tube, the ion is handed over
Change fiber and multi-section serial is carried out with this, every layer of subregion filter plate is fixed between the central support tube and the cylinder.
The filter material of wherein described subregion filter plate is divided evenly into 6 subregions using filter.
Advantageously, Inlet and outlet water upper and lower ends are in charge of carry out uniform water distribution using ring, when ring is in charge of filtering, from the cylinder
Body bottom intakes, upper end water outlet；During regeneration, from cylinder upper end water inlet, lower end draining.
Advantageously, it is in hollow cylinder that the ring, which is in charge of overall, and wherein one end is closed, and is in charge of circumferential uniform point of cylinder along ring
It is furnished with multiple water distributing pores, ring is in charge of by blind end towards being arranged at cylinder two ends in the way of in cylinder.
The ion-exchange fibre device of multi-section serial in the utility model can be with other multi-section serials ion exchange
Fiber plant has the connected mode of diversified forms, the form such as including series, parallel.
This structure of the present utility model effectively improves ion fiber filtration resistance greatly, the situation of operational effect difference, together
When increase discharge capacity so that use ion exchange technique, using big flow, the method for operation of skinny device is achieved, solve
Conventional use ion exchange pot floor space of having determined is big, and the problem of flow is small reduces operating cost.
Brief description of the drawings
In order to be easier to understand the technical solution of the utility model and beneficial technique effect, by referring to showing in the accompanying drawings
The application is described in detail for the embodiment of the present utility model that goes out.The accompanying drawing depict only the allusion quotation of the application
Type embodiment, does not constitute the limitation to the protection domain of the application, wherein：
Fig. 1 is illustrated according to the multi-section serial ion-exchange fibre apparatus structure of an embodiment of the present utility model
Figure.
Fig. 2 a and 2b are the multi-section serial ion-exchange fibre device according to an embodiment of the present utility model respectively
Subregion filter plate front view and top view.
Fig. 3 a and 3b are the multi-section serial ion-exchange fibre device according to an embodiment of the present utility model respectively
The vertical and horizontal sectional view be in charge of of ring.
In the reference indicated in these figures：
1：Cylinder；2：Clip；3：Sealing ring：4：Seam flange；5：End socket；6：Ring is in charge of；7：Bolt；8：Sealing ring；9：
Subregion filter plate；10：Ion-exchange fibre；11：Central support tube；12：Pipe plug；13：Water distributing pore.
Embodiment
Fig. 1 is shown to be shown according to the multi-section serial ion-exchange fibre apparatus structure of an embodiment of the present utility model
It is intended to.The multi-section serial ion-exchange fibre device is made with pillar cylinder 1 and central support tube 11 with certain bearing capacity
For agent structure, the two ends pipe plug 12 of central support tube 11 is blocked, and ion is filled between the cylinder 1 and central support tube 11
Exchange fiber 10, layering, the ion exchange are separated between the cylinder 1 and the central support tube 11 by subregion filter plate 9
Fiber 10 carries out multi-section serial with this, and every layer of subregion filter plate 9 is fixed between the central support tube 11 and the cylinder 1.
As shown in figures 2 a and 2b, filter material is divided evenly into 6 subregions, filter to the structure of the subregion filter plate 9 using filter
Play support fiber, when preventing big hydraulic blow, fibre leakage.The skeleton of 6 subregions, supports filter, further for fixed
Prevent because big hydraulic blow filter deforms damaged, fibre leakage.
The upper and lower side of the cylinder 1 is connected with end socket 5, and end socket 5 is fixed on the two ends of cylinder 1 by clip 2, in cylinder 1
Inward flange is provided with seam flange 4, and seam flange 4 is fixed on subregion filter plate 9 by bolt 7, plays the subregion filter of fixed series connection
Framework is acted on.Sealing ring 3 is located at the upper end of cylinder 1, compresses and sealed cylinder 1 and end socket 5, prevents because being sealed not when pressure is excessive
Sternly, filtered fluid is leaked.Sealing ring 8 is located at subregion filter plate sidepiece, and increasing rubs with cylinder 1, and segmentation is each jointly with subregion filter plate 9
Filter layer.Ring is respectively arranged with the end socket 5 of the upper and lower ends of cylinder 1 it is in charge of in 6, Fig. 3 a and 3b and shows the structure that ring is in charge of 6, ring
It is in hollow cylinder to be in charge of 6 entirety, and wherein one end is closed, and is in charge of 6 cylinders along ring and is circumferentially evenly distributed with multiple water distributing pores 13, ring
It is in charge of 6 by blind end towards being arranged on the end socket 5 of upper and lower side in the way of in cylinder, during water inlet, current are in charge of 6 sidepieces from ring
Water distributing pore 13 is flowed into, into the fibrous layer 10 in cylinder 1., using ring be in charge of 6 reduce big flow intake when hydraulic blow,
Water distributing pore can reach the purpose of uniform water distribution, during filtering, from the water inlet of cylinder bottom, upper end water outlet；During regeneration, from cylinder
Upper end intakes, lower end draining.
The utility model can be embodied in other specific forms, but without departing from protection model of the present utility model
Enclose, protection domain of the present utility model is defined only by the following claims.
Claims (5)
1. a kind of multi-section serial ion-exchange fibre device, it is with pillar cylinder and central support tube with certain bearing capacity
As agent structure, central support tube two ends are blocked with pipe plug, and ion exchange is filled between the cylinder and central support tube
Fiber, it is characterised in that layering, the ion exchange are separated by subregion filter plate between the cylinder and the central support tube
Fiber carries out multi-section serial with this, and every layer of subregion filter plate is fixed between the central support tube and the cylinder.
2. multi-section serial ion-exchange fibre device according to claim 1, wherein the filter material of the subregion filter plate is used
Filter equably 6 subregions.
3. multi-section serial ion-exchange fibre device according to claim 1, wherein Inlet and outlet water upper and lower ends use ring
It is in charge of carry out uniform water distribution, during filtering, from cylinder bottom water inlet, upper end water outlet；During regeneration, from the cylinder upper end
Water inlet, lower end draining.
4. multi-section serial ion-exchange fibre device according to claim 3, wherein it is in open circles that the ring, which is in charge of overall,
Cylindricality, wherein one end are closed, and being in charge of cylinder along ring is circumferentially evenly distributed with multiple water distributing pores, and ring is in charge of with blind end towards cylinder
Interior mode is arranged at cylinder two ends.
5. the multi-section serial ion-exchange fibre device according to any one of claim 1-4, the wherein multi-section serial from
Sub- exchange fiber device connected in series or in parallel can be used with multiple.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720096046.7U CN206467005U (en) | 2017-01-25 | 2017-01-25 | A kind of multi-section serial ion-exchange fibre device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720096046.7U CN206467005U (en) | 2017-01-25 | 2017-01-25 | A kind of multi-section serial ion-exchange fibre device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206467005U true CN206467005U (en) | 2017-09-05 |
Family
ID=59704486
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720096046.7U Active CN206467005U (en) | 2017-01-25 | 2017-01-25 | A kind of multi-section serial ion-exchange fibre device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206467005U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20210371293A1 (en) * | 2018-10-18 | 2021-12-02 | Geolith | Installation and Method for Separating at Least One Ionic Species from a Solution Comprising at Least Said Ionic Species and Lithium |
-
2017
- 2017-01-25 CN CN201720096046.7U patent/CN206467005U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20210371293A1 (en) * | 2018-10-18 | 2021-12-02 | Geolith | Installation and Method for Separating at Least One Ionic Species from a Solution Comprising at Least Said Ionic Species and Lithium |
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| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 301800 No.10, Fuli Road, plastic products industrial zone, Baodi District, Tianjin Patentee after: Oseco membrane technology (Tianjin) Co.,Ltd. Address before: 301800 No.10, Fuli Road, plastic products industrial zone, Baodi District, Tianjin Patentee before: TIANJIN BISHUIYUAN MEMBRANE MATERIAL Co.,Ltd. |