CN204873944U - Co current regeneration anion exchange ware - Google Patents
Co current regeneration anion exchange ware Download PDFInfo
- Publication number
- CN204873944U CN204873944U CN201520563774.5U CN201520563774U CN204873944U CN 204873944 U CN204873944 U CN 204873944U CN 201520563774 U CN201520563774 U CN 201520563774U CN 204873944 U CN204873944 U CN 204873944U
- Authority
- CN
- China
- Prior art keywords
- water
- piping
- tank body
- port
- discharge piping
- 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
- 230000008929 regeneration Effects 0.000 title claims abstract description 15
- 238000011069 regeneration method Methods 0.000 title claims abstract description 15
- 238000005349 anion exchange Methods 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 150000001450 anions Chemical class 0.000 claims description 12
- 239000011347 resin Substances 0.000 claims description 11
- 229920005989 resin Polymers 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 6
- 238000013022 venting Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 abstract 6
- 239000003381 stabilizer Substances 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000005516 engineering process 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
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000012492 regenerant Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model relates to a co current regeneration anion exchange ware, including jar body and a stabilizer blade, the top of jar body is equipped with into water piping and exhaust piping, and the bottom of jar body is equipped with the discharge piping, the inlet tube is fastened to hold to have and is located a jar internal water installations, water installations has strip -type through hole's cylinder for the surface, and the lower extreme level of the piping of intaking is provided with water inlet and backwash outlet, and the inlet tube is fastened and is equipped with into regeneration liquid mouth, the upper end level of discharge piping is provided with delivery port and backwash water inlet, and the discharge piping middle section is equipped with just washes the outlet, and the discharge piping lower extreme has and is located a jar internal play water installation, go out the water installation has the apopore for the centre arc, exhaust piping middle section is equipped with the ball valve, and its lower extreme is the relief port. The utility model discloses improve water installations and go out the water installation on the basis of existing equipment for whole equipment also can adopt under the raw water quality condition poor slightly, can save the processing time greatly and practice thrift the cost.
Description
Technical field
The utility model relates to water technology apparatus field, especially a kind of co-current regeneration anion exchanger.
Background technology
Co-current regeneration anion exchanger is applicable to water softening or desalination, and interchanger main body is an airtight former cylindrical shell, is provided with water feed apparatus, water-freeing arrangement, enters regenerated liquid device, and load the ion exchange resin of certain altitude in body.Existing co-current regeneration effluent quality is bad, and regeneration specific consumption is high, therefore only or contact when regenerating employing good especially at raw water quality, but it is simple to operate, if its structure can be changed, make it also can adopt when raw water quality is slightly poor, greatly can save treatment time and cost-saving.
Utility model content
The technical problems to be solved in the utility model is: based on the problems referred to above, provides a kind of co-current regeneration anion exchanger.
The utility model solves the technical scheme that its technical problem adopts: a kind of co-current regeneration anion exchanger, comprise tank body and leg, the top of described tank body is provided with into water piping and exhaust piping, the bottom of tank body is provided with discharge piping, described water inlet pipe is fastened end and is had the water feed apparatus being positioned at tank body, described water feed apparatus is the right cylinder that outside surface has strip through hole, the lower end of water inlet piping has been horizontally disposed with water-in and backwash water port, water inlet pipe is fastened and is provided with into regenerated liquid mouth, the upper end of described discharge piping has been horizontally disposed with water outlet and backwash water-in, discharge piping stage casing is provided with just washes water port, discharge piping lower end has the discharging device being positioned at tank body, described discharging device is the arc that centre has posticum, described exhaust piping stage casing is provided with ball valve, its lower end is venting port.
Further, described tank body top is provided with resin overside port, two visors and upper manhole, and tank body lower part is provided with lower resin overside port and lower manhole.
Further, the lower end of described water inlet piping and discharge piping is provided with tensimeter.
Further, described water-in, backwash water port, enter regenerated liquid mouth, water outlet, backwash water-in and just washing in water port and be all connected with diaphragm valve.
The beneficial effects of the utility model are: the utility model improves water feed apparatus and discharging device on the basis of existing equipment, and whole equipment also can be adopted when raw water quality is slightly poor, greatly can save treatment time and cost-saving.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the right view of Fig. 1.
In figure: 1. tank body, 2. leg, 3. intake piping, 4. exhaust piping, 5. discharge piping, 6. water feed apparatus, 7. water-in, 8. backwash water port, 9. enter regenerated liquid mouth, 10. water outlet, 11. backwash water-ins, 12. just wash water port, 13. discharging devices, 14. ball valves, 15. venting ports, resin overside port on 16., 17. visors, manhole on 18., 19. times resin overside ports, 20. times manholes, 21. tensimeters, 22. diaphragm valves.
Embodiment
By reference to the accompanying drawings the utility model is described in further detail now.These accompanying drawings are the schematic diagram of simplification, only basic structure of the present utility model are described in a schematic way, and therefore it only shows the formation relevant with the utility model.
As shown in Fig. 1 ~ 2, a kind of co-current regeneration anion exchanger, comprise tank body 1 and leg 2, the top of tank body 1 is provided with into water piping 3 and exhaust piping 4, the bottom of tank body 1 is provided with discharge piping 5, water inlet piping 3 upper end has the water feed apparatus 6 being positioned at tank body 1, water feed apparatus 6 has the right cylinder of strip through hole for outside surface, the lower end of water inlet piping 3 has been horizontally disposed with water-in 7 and backwash water port 8, water inlet piping 3 is provided with into regenerated liquid mouth 9, the upper end of discharge piping 5 has been horizontally disposed with water outlet 10 and backwash water-in 11, discharge piping 5 stage casing is provided with just washes water port 12, discharge piping 5 lower end has the discharging device 13 being positioned at tank body 1, discharging device 13 is the middle arc with posticum, exhaust piping 4 stage casing is provided with ball valve 14, its lower end is venting port 15.Tank body 1 top is provided with resin overside port 16, two visors 17 and upper manhole 18, and tank body 1 bottom is provided with lower resin overside port 19 and lower manhole 20.The lower end of water inlet piping 3 and discharge piping 4 is provided with tensimeter 21.Water-in 7, backwash water port 8, enter regenerated liquid mouth 9, water outlet 10, backwash water-in 11 and just washing in water port 12 to be all connected with diaphragm valve 22.
Schedule of operation is described below: 1. small reverse washing: object is the suspended impurity in cleaning packed resin layer, when anion exchanger is arranged on after reverse osmosis, because water inlet is very clean, so small reverse washing need not all carry out at every turn, carries out a small reverse washing after can running ten times; 2. discharge water: backwash water therefrom enters interchanger, discharge from interchanger top, backwash, to going out clarification of water, generally needs within 10 ~ 15 minutes, to open middle valve door and drain tap, is released by water more than middle comb, till anhydrous in middle comb by middle comb; 3. anion regenerant interchanger enters sodium hydroxide: with the speed of about void tower flow velocity 5m/h, regenerated liquid is flow through resin layer from bottom to top, discharged by middle comb; 4. just wash: comb in closedown, open water intaking valve, after waiting vent valve water outlet, open lower valve, close vent valve.Resin is just washed, identical when flow velocity and dynamic row, until effluent quality meets the requirements.Output water valve, close lower valve, normal operation input.
With above-mentioned according to desirable embodiment of the present utility model for enlightenment, by above-mentioned description, relevant staff in the scope not departing from this utility model technological thought, can carry out various change and amendment completely.The technical scope of this utility model is not limited to the content on specification sheets, must determine its technical scope according to right.
Claims (4)
1. a co-current regeneration anion exchanger, comprise tank body (1) and leg (2), it is characterized in that: the top of described tank body (1) is provided with into water piping (3) and exhaust piping (4), the bottom of tank body (1) is provided with discharge piping (5), described water inlet piping (3) upper end has the water feed apparatus (6) being positioned at tank body (1), described water feed apparatus (6) has the right cylinder of strip through hole for outside surface, the lower end of water inlet piping (3) has been horizontally disposed with water-in (7) and backwash water port (8), water inlet piping (3) is provided with into regenerated liquid mouth (9), the upper end of described discharge piping (5) has been horizontally disposed with water outlet (10) and backwash water-in (11), discharge piping (5) stage casing is provided with just washes water port (12), discharge piping (5) lower end has the discharging device (13) being positioned at tank body (1), described discharging device (13) is the middle arc with posticum, described exhaust piping (4) stage casing is provided with ball valve (14), its lower end is venting port (15).
2. a kind of co-current regeneration anion exchanger according to claim 1, it is characterized in that: described tank body (1) top is provided with resin overside port (16), two visors (17) and upper manhole (18), tank body (1) bottom is provided with lower resin overside port (19) and lower manhole (20).
3. a kind of co-current regeneration anion exchanger according to claim 1, is characterized in that: the lower end of described water inlet piping (3) and discharge piping (5) is provided with tensimeter (21).
4. a kind of co-current regeneration anion exchanger according to claim 1, is characterized in that: described water-in (7), backwash water port (8), enter regenerated liquid mouth (9), water outlet (10), backwash water-in (11) and just washing in water port (12) to be all connected with diaphragm valve (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520563774.5U CN204873944U (en) | 2015-07-30 | 2015-07-30 | Co current regeneration anion exchange ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520563774.5U CN204873944U (en) | 2015-07-30 | 2015-07-30 | Co current regeneration anion exchange ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204873944U true CN204873944U (en) | 2015-12-16 |
Family
ID=54818343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520563774.5U Expired - Fee Related CN204873944U (en) | 2015-07-30 | 2015-07-30 | Co current regeneration anion exchange ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204873944U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542609A (en) * | 2016-10-25 | 2017-03-29 | 芜湖东旭光电科技有限公司 | Soften resin regeneration method, system and the method using the system regeneration resin |
-
2015
- 2015-07-30 CN CN201520563774.5U patent/CN204873944U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542609A (en) * | 2016-10-25 | 2017-03-29 | 芜湖东旭光电科技有限公司 | Soften resin regeneration method, system and the method using the system regeneration resin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20151216 Termination date: 20160730 |