CN208912091U - Ion exchange column - Google Patents
Ion exchange column Download PDFInfo
- Publication number
- CN208912091U CN208912091U CN201821143620.0U CN201821143620U CN208912091U CN 208912091 U CN208912091 U CN 208912091U CN 201821143620 U CN201821143620 U CN 201821143620U CN 208912091 U CN208912091 U CN 208912091U
- Authority
- CN
- China
- Prior art keywords
- ion exchange
- shell
- exchange column
- column according
- pillar
- 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.)
- Expired - Fee Related
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a kind of ion exchange column, including shell, and the inner vertical of shell is through there is pillar, and the outside of pillar is from top to bottom sequentially arranged at intervals with multiple halo ion power boards, and halo ion power board is provided with diversion pipe close to the bottom of inner edge;Feed inlet is provided at the top of shell, the bottom of shell is provided with discharge port.The ion exchange column can be carried out efficiently ion exchange.
Description
Technical field
The utility model relates to a kind of ion exchange columns.
Background technique
Ion exchange column refers to the column pressure vessel for carrying out ion-exchange reactions, is the friendship of tubing string method ion exchange
Exchange device.Using cylinder-shaped exchange column, solution is passed through from one end of column, with the fixed ion exchanger resin in column being in dense state
Layer or flow regime ion exchange resin bed come into full contact with, and carry out ion exchange.If the solution after exchange has reached pre-provisioning request,
Or ion exchange resin has been in " saturation state ", and column exchange is just cut off from production line, with solution in same column or in other columns
Imbibition desorbs, for exchange next time after ion exchange resin regeneration.Using ion exchange column, it is equivalent to amberlite in column
Multiple batches of swap with solution of rouge point is reacted, and the solution after exchange is separated with ion exchange resin in time.Flow through ion exchange
The solution composition of resin bed changes with bed height at any time.
Existing ion exchange column is the inside that exchanger resin is filled to pillar, although this mode passes through exchange
Resin large number of and reached raising exchange efficiency, but economically and from the flow rate of fluid consider,
Cost and the efficiency needs of the ion exchange column further increase.
Utility model content
The purpose of the utility model is to provide a kind of ion exchange column, which can be carried out efficiently ion friendship
It changes.
To achieve the goals above, the utility model provides a kind of ion exchange column, including shell, and the inside of shell is perpendicular
Directly through there is pillar, the outside of pillar is from top to bottom sequentially arranged at intervals with multiple halo ion power boards, halo ion exchange
Plate is provided with diversion pipe close to the bottom of inner edge;Feed inlet is provided at the top of shell, the bottom of shell is provided with discharge port.
Preferably, pillar is shaft, and the end of pillar is provided with driving unit, and driving unit is set to the top of shell
The bottom and/or.
Preferably, driving unit is rotary electric machine.
Preferably, halo ion power board tilts gradually downward from the direction of the outside of shell internally.
Preferably, the direction from the outside of shell internally, diversion pipe gradually tilt upwards.
Preferably, halo ion power board include the upper hollowed-out board from top to bottom set gradually, ion exchange resin and under
Hollowed-out board.
Preferably, shell is from top to bottom sequentially connected by multiple pipeline sections, is connected between adjacent pipeline section by flange.
Preferably, the outside of shell is provided with reinforcing rib.
Preferably, the end of shell is hemispherical dome structure.
In the above-mentioned technical solutions, the working principle of ion exchange column provided by the utility model is as follows: firstly, liquid is certainly
Feed inlet enters the inside of shell, and the halo ion power board for initially entering the first floor under gravity carries out ion exchange,
It will pass through the carry out Two-step ion-exchanging that diversion pipe is delivered to next layer of halo ion power board after ion exchange, and so on
It is finally discharged into excessively multiple ion exchange from discharge port so as to complete ion exchange.As can be seen from the above description, in this reality
In novel, which realizes rapidly ion exchange by using less exchanger resin.
Other feature and advantage of the utility model will the following detailed description will be given in the detailed implementation section.
Detailed description of the invention
Attached drawing is to be used to provide a further understanding of the present invention, and constitute part of specification, and following
Specific embodiment be used to explain the utility model together, but do not constitute limitations of the present invention.In the accompanying drawings:
Fig. 1 is the structural schematic diagram of the preferred embodiment of ion exchange column provided by the utility model.
Description of symbols
1, shell 2, pillar
3, halo ion power board 4, diversion pipe
5, driving unit 6, feed inlet
7, discharge port 8, reinforcing rib
9, flange
Specific embodiment
Specific embodiment of the present utility model is described in detail below in conjunction with attached drawing.It should be understood that herein
Described specific embodiment is only used for describing and explaining the present invention, and is not intended to limit the utility model.
In the present invention, in the absence of explanation to the contrary, the side that " upper and lower, inside and outside " etc. is included in the term
Position word only represent orientation of the term under normal service condition, or be those skilled in the art understand that be commonly called as, without that should regard
For the limitation to the term.
The utility model provides a kind of ion exchange column, including shell 1, and the inner vertical of shell 1, which runs through, pillar 2,
The outside of pillar 2 is from top to bottom sequentially arranged at intervals with multiple halo ion power boards 3, and halo ion power board 3 is close to inner edge
Bottom be provided with diversion pipe 4;The top of shell 1 is provided with feed inlet 6, and the bottom of shell 1 is provided with discharge port 7.
The working principle of above-mentioned ion exchange column is as follows: firstly, liquid enters the inside of shell 1 from feed inlet 6, in weight
The halo ion power board 3 that the first floor is initially entered under the action of power carries out ion exchange, and it is defeated to will pass through diversion pipe 4 after ion exchange
Send to the carry out Two-step ion-exchanging of next layer of halo ion power board 3, and so on it is final into excessively multiple ion exchange
It is discharged from discharge port 7 so as to complete ion exchange.As can be seen from the above description, in the present invention, the ion exchange column
Rapidly ion exchange is realized by using less exchanger resin.
In the present invention, pillar 2 can be fixed, may be set to be rotation, in order to further mention
The rate of macroion exchange, it is preferable that pillar 2 is shaft, and the end of pillar 2 is provided with driving unit 5, and driving unit 5 is arranged
In the top and/or bottom of shell 1.Thus pillar 2 can be driven to rotate around vertical direction by driving unit 5, in centrifugal force
Under the action of so improve liquid ion slow down rate.
In the above-described embodiment, the specific type of driving unit 5 can select in a wide range, such as hydraulic pump,
But consider from cost and in operation convenience, it is preferable that driving unit 5 is rotary electric machine.
In the above-described embodiment, halo ion power board 3 can be plane setting, be also possible to be obliquely installed, still
In order to further increase the rate of ion exchange, it is preferable that direction of the halo ion power board 3 from the outside of shell 1 internally
It tilts gradually downward.By being obliquely installed, by the ion exchange that can further increase liquid under the effect of gravity
Rate.
In the case of halo ion power board 3 is obliquely installed, in order to further increase liquid flow to next layer of ring-type from
Sub- power board 3, it is preferable that from the direction of the outside of shell 1 internally, the gradually inclination upwards of diversion pipe 4.
In the present invention, the specific structure of halo ion power board 3 can select in a wide range, but in order to
Further increase the contact area of liquid and ion exchange resin, it is preferable that halo ion power board 3 includes from top to bottom successively
Upper hollowed-out board, ion exchange resin and the lower hollowed-out board being arranged.
In the present invention, in order to further increase the packaging efficiency of shell 1, it is preferable that shell 1 by multiple pipeline sections by
It is sequentially connected under above, is connected between adjacent pipeline section by flange 9.
In the present invention, it is contemplated that the intensity for the power that shell 1 is subject to during the work time, it is outer in order to further increase
The mechanical strength of shell 1, it is preferable that the outside of shell 1 is provided with reinforcing rib 8.Wherein, in order to further increase the machinery of shell 1
Intensity, it is highly preferred that the end of shell 1 is hemispherical dome structure.
Preferred embodiments of the present invention, still, the utility model and unlimited are described in detail in conjunction with attached drawing above
Detail in above embodiment can be to the skill of the utility model in the range of the technology design of the utility model
Art scheme carries out a variety of simple variants, these simple variants belong to the protection scope of the utility model.
It is further to note that specific technical features described in the above specific embodiments, in not lance
It in the case where shield, can be combined in any appropriate way, in order to avoid unnecessary repetition, the utility model is to each
No further explanation will be given for the possible combination of kind.
In addition, any combination can also be carried out between a variety of different embodiments of the utility model, as long as it is not disobeyed
The thought for carrying on the back the utility model, equally should be considered as content disclosed in the utility model.
Claims (9)
1. a kind of ion exchange column, which is characterized in that including shell (1), the inner vertical of the shell (1), which runs through, pillar
(2), the outside of the pillar (2) is from top to bottom sequentially arranged at intervals with multiple halo ion power boards (3), the halo ion
Power board (3) is provided with diversion pipe (4) close to the bottom of inner edge;It is provided with feed inlet (6) at the top of the shell (1), it is described
The bottom of shell (1) is provided with discharge port (7).
2. ion exchange column according to claim 1, which is characterized in that the pillar (2) is shaft, the pillar (2)
End be provided with driving unit (5), the driving unit (5) is set to the top and/or bottom of the shell (1).
3. ion exchange column according to claim 2, which is characterized in that the driving unit (5) is rotary electric machine.
4. ion exchange column according to claim 1, which is characterized in that the halo ion power board (3) is from described outer
The direction of the outside of shell (1) internally tilts gradually downward.
5. ion exchange column according to claim 4, which is characterized in that from the side of the outside of the shell (1) internally
To the diversion pipe (4) gradually inclination upwards.
6. ion exchange column according to claim 1, which is characterized in that the halo ion power board (3) includes by upper
Upper hollowed-out board, ion exchange resin and the lower hollowed-out board set gradually under and.
7. ion exchange column according to claim 1, which is characterized in that the shell (1) by multiple pipeline sections from top to bottom
It is sequentially connected, is connected between the adjacent pipeline section by flange (9).
8. ion exchange column according to claim 1, which is characterized in that the outside of the shell (1) is provided with reinforcing rib
(8)。
9. ion exchange column according to claim 1, which is characterized in that the end of the shell (1) is hemispherical dome structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821143620.0U CN208912091U (en) | 2018-07-19 | 2018-07-19 | Ion exchange column |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821143620.0U CN208912091U (en) | 2018-07-19 | 2018-07-19 | Ion exchange column |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208912091U true CN208912091U (en) | 2019-05-31 |
Family
ID=66694318
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201821143620.0U Expired - Fee Related CN208912091U (en) | 2018-07-19 | 2018-07-19 | Ion exchange column |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208912091U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108786932A (en) * | 2018-07-19 | 2018-11-13 | 芜湖福民生物药业股份有限公司 | ion exchange column |
-
2018
- 2018-07-19 CN CN201821143620.0U patent/CN208912091U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108786932A (en) * | 2018-07-19 | 2018-11-13 | 芜湖福民生物药业股份有限公司 | ion exchange column |
CN108786932B (en) * | 2018-07-19 | 2024-03-19 | 芜湖福民生物药业股份有限公司 | Ion exchange column |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201046396Y (en) | Non-rotary vertical cyclic liquid knockout reactor | |
CN208912091U (en) | Ion exchange column | |
CN204265488U (en) | Exchange resin tower | |
CN108079752A (en) | A kind of multistage cross flow-adverse current liquid distributor for rotary filling bed and its application | |
CN106825020A (en) | Soil repair system and method that a kind of materialization is combined | |
CN210122563U (en) | Mixing arrangement is used in plant essential oil extraction | |
CN205759800U (en) | Combined type Multi-stage rotary packed bed mass transfer reaction device | |
CN206613397U (en) | A kind of sewage disposal air lift negative pressure dosing agitating device | |
CN108786932A (en) | ion exchange column | |
CN204735153U (en) | High -speed vertical circulation mixer | |
CN105275445B (en) | Concentric pipe type foam generator | |
CN107096250A (en) | High-purity chemical products purification system | |
CN110242532A (en) | A kind of low level degree liquid lever electrodynamic type draw-out device | |
CN206381996U (en) | A kind of hydrogenation reaction cauldron | |
CN107998921A (en) | A kind of nursery soil application mixing arrangement | |
CN102897854B (en) | Water purifier dosing device | |
CN105854332B (en) | Combined type Multi-stage rotary packed bed mass transfer reaction device and its reaction method of completion | |
CN215275866U (en) | Internal circulation countercurrent extraction tower | |
CN211886426U (en) | Chemical industry is with high-efficient mixer of axis ventilating | |
WO2019056826A1 (en) | Extraction device having compact structure | |
CN108043191A (en) | A kind of device and method of Sodium/Calcium dual alkali scrubbing FGD process | |
CN206970565U (en) | A kind of bleacher | |
CN203842593U (en) | Ion exchange column for purifying tocopherol succinate | |
CN210653858U (en) | Electrical heating formula beverage liquid filling machine | |
CN103638855B (en) | A kind of waste liquid pool agitating device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190531 Termination date: 20200719 |
|
CF01 | Termination of patent right due to non-payment of annual fee |