CN203700077U - Efficient ion exchanger - Google Patents
Efficient ion exchanger Download PDFInfo
- Publication number
- CN203700077U CN203700077U CN201420064528.0U CN201420064528U CN203700077U CN 203700077 U CN203700077 U CN 203700077U CN 201420064528 U CN201420064528 U CN 201420064528U CN 203700077 U CN203700077 U CN 203700077U
- Authority
- CN
- China
- Prior art keywords
- tank body
- water
- water inlet
- inlet pipe
- filter plate
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- 230000000630 rising effect Effects 0.000 claims abstract description 33
- 239000011347 resin Substances 0.000 claims abstract description 25
- 229920005989 resin Polymers 0.000 claims abstract description 25
- 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 claims abstract description 23
- 239000003456 ion exchange resin Substances 0.000 claims abstract description 23
- 229920003303 ion-exchange polymer Polymers 0.000 claims abstract description 23
- 238000005192 partition Methods 0.000 claims abstract description 14
- 238000011010 flushing procedure Methods 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 13
- 230000008093 supporting effect Effects 0.000 claims description 4
- 241000282326 Felis catus Species 0.000 claims description 2
- -1 filter plate Substances 0.000 claims description 2
- 238000007689 inspection Methods 0.000 claims description 2
- 230000008929 regeneration Effects 0.000 description 18
- 238000011069 regeneration method Methods 0.000 description 18
- 238000000034 method Methods 0.000 description 9
- 239000012535 impurity Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000009388 chemical precipitation Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000001976 improved effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000012492 regenerant Substances 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Abstract
The utility model provides an efficient ion exchanger. The efficient ion exchanger comprises a tank body, a vertical partition board, an ion exchange resin, a filter plate, water caps, a water inlet pipe and a water outlet pipe, wherein the tank body is divided into two parts by the vertical partition board, the filter plate is mounted in the hollow cavity of the tank body, the water caps are mounted on the filter plate, the hollow cavity of the tank body is filled with the ion exchange resin and the ion exchange resin is positioned below the filter plate, and the water inlet pipe and the water outlet pipe are arranged on the two sides of the vertical partition board and at the upper part of the tank body; when the ion exchanger is in normal operation, raw water flows to the upper layer space of the ion exchange resin through the water caps and the filter plate from the water inlet pipe, the water flowing manner in the ion exchange resin is that the water is pressed downwards firstly, and then returned back for rising, and the raw water flows out of the tank body through the water caps, the filter plate and the water outlet pipe after flowing through the ion exchange resin. According to the efficient ion exchanger, the problems that the water inlet and the water outlet of the exchanger are easy to block and the resin is easy to harden are solved; meanwhile, the efficient ion exchanger has the advantages that the water preparing amount can be increased greatly, the design is reasonable, and the ion exchanger is convenient and practical.
Description
Technical field
The utility model is a kind of high-efficiency ion exchanger, and particularly a kind of high-efficiency ion exchanger for heavy metal wastewater thereby suite of equipment belongs to the renovation technique of high-efficiency ion exchanger.
Background technology
Process for treating heavy-metal waste water is a lot, mainly contains chemical precipitation method, ion exchange method, iron replacement method and ferrite process etc.Wherein chemical precipitation method use is the most general, and the metal being worth containing higher reclamation, as the wastewater treatment of nickel, chromium etc., the ion exchange methods that adopt more.
Apply the form that comparatively general ion-exchanger generally adopts co-current regeneration formula fixed bed, counter-current regeneration formula fixed bed and backhaul ion-exchanger.In co-current regeneration formula fixed bed, the flow direction of regenerator is identical with flowing to of processed water, and when regeneration, from front end to rear end, resin saturation ratio and regenerated liquid concentration all reduce gradually, cause rear end resin regeneration weak effect, and system regeneration liquid consumption is large.Its recovery stream of counter-current regeneration formula fixed bed, to contrary with the operation flow direction, has favorable regeneration effect, the advantage that regenerated liquid consumption is few.But disorderly layer phenomenon of resin easily occurs counter-current regeneration formula fixed bed, for avoiding it to occur, need to adopt pneumatic jack, water top or reduce the methods such as operation flow velocity, thereby occurring equipment and complicated operation, the problem such as water loss is large, plant factor is low.
Return stroke type softener is to have set up vertical partition plate in the middle of cylindrical body, by rounded section in two.Fluid enters and flows downward from a upper lateral part, turns to opposite side upwards to flow again from the lower partition, flows out from the top of this side, is so backhaul form by resin layer, and its regeneration is counter-current regeneration.Push down resin because current enter top, thereby can not produce disorderly layer phenomenon.Return stroke type softener has been inherited all advantage of counter-current regeneration formula fixed bed, has overcome again the easily shortcoming of random layer of resin, easy and simple to handle, needn't strictly control regeneration velocity, and body height is little, simple in structure.
The inlet tube and outlet tube of traditional return stroke type softener and small reverse washing water inlet pipe all use filter screen wrapping, and than the form of filter plate+water cap of fixed bed, its flow area greatly reduces.In the time that water inlet contains more suspended substance and silt, impurity, easily there is the problem of stopping up.Tiny silt and mud easily enters in interchanger by filter screen simultaneously, and forms piece with resin, because water flow mode is for first pressing down, then upper punch, backwash intensity is difficult for promoting, and while causing backwash, mud cannot depart from from resin surface.In the course of time, resin layer resistance is increased, discharge reduction processed because mud is wrapped in resin, makes resin regeneration incomplete simultaneously, has not only wasted a large amount of regenerators, and has shortened water production in periodic mode.
Summary of the invention
The purpose of this utility model is to consider the problems referred to above and high-efficiency ion exchanger that a kind of easy blockage problem of intake-outlet that has solved interchanger is provided.The utility model can increase the water yield processed greatly, reasonable in design, convenient and practical.
The technical solution of the utility model is: high-efficiency ion exchanger of the present utility model, include tank body, vertical partition plate, ion exchange resin, filter plate, water cap, water inlet pipe, rising pipe, tank body is separated into two portions by vertical partition plate, filter plate is installed in the hollow cavity of tank body, water cap is installed on filter plate, ion exchange resin is installed in the hollow cavity of tank body, and be positioned at the below of filter plate, the top of tank body is respectively equipped with water inlet pipe and rising pipe in the both sides of vertical partition plate, when normal operation former water from water inlet pipe through water cap, filter plate enters the upper sheaf space of ion exchange resin, water inlet is first to press down the rising of turning back again in the mistake stream mode of ion exchange resin, former water flows through after ion exchange resin again through water cap, filter plate and rising pipe flow out tank body.
Above-mentioned water inlet pipe in the time of back flushing as back flushing rising pipe, rising pipe in when recoil as back flushing water inlet pipe, back flushing feed water flow to former water feed water flow to contrary, flow into tank body from rising pipe, flow out from water inlet pipe.
Compared with prior art, tool has the following advantages the utility model:
1) the utility model has improved traditional return stroke type softener, intake-outlet has adopted filter plate to install the form of water cap additional, with respect to the form of traditional filter screen wrapping water inlet pipe and water outlet pipe, flow area increases mutually greatly, and sheaf space is larger on filter plate, impurity and silt are had to certain carrying capacity, and when back flushing, impurity and silt are easily discharged, thereby the intake-outlet that has solved traditional return stroke type softener holds susceptible to plugging problem;
2) back flushing water inlet pipe is set up in interchanger of the present utility model bottom, with respect to first pressing down of traditional return stroke type softener, the water flow mode of upper punch again, backwash intensity lift-rising greatly, thereby can effectively clean suspended substance and the mud of resin surface deposition and cut-off filter, thereby solve that influent turbidity is high, silt and impurity is when many, the problem that resin easily hardens.
The utility model is that a kind of design is ingenious, excellent property, convenient and practical high-efficiency ion exchanger.
Brief description of the drawings
Fig. 1 is vertical view of the present utility model;
Fig. 2 is the A-A sectional view in Fig. 1;
Fig. 3 is the structural representation of filter plate in the utility model.
Embodiment
Embodiment:
Structural representation of the present utility model is as Fig. 1, 2, shown in 3, high-efficiency ion exchanger of the present utility model, it is characterized in that including tank body 1, vertical partition plate 2, ion exchange resin 3, filter plate 4, water cap 5, water inlet pipe 6, rising pipe 7, tank body 1 is separated into left and right two portions by vertical partition plate 2, filter plate 4 is installed in the hollow cavity of tank body 1, water cap 5 is installed on filter plate 4, ion exchange resin 3 is installed in the hollow cavity of tank body 1, and be positioned at the below of filter plate 4, the top of tank body 1 is respectively equipped with water inlet pipe 6 and rising pipe 7 in the both sides of vertical partition plate 2, when normal operation former water from water inlet pipe 6 through water cap 5, filter plate 4 enters the upper sheaf space of ion exchange resin 3, water inlet is first to press down the rising of turning back again in the mistake stream mode of ion exchange resin 3, former water flows through after ion exchange resin 3 again through water cap 5, filter plate 4 and rising pipe 7 flow out tank body 1.
In the present embodiment, above-mentioned water inlet pipe 6 in the time of back flushing as back flushing rising pipe, rising pipe 7 in when recoil as back flushing water inlet pipe, back flushing feed water flow to former water feed water flow to contrary, flow into tank body from rising pipe 7, flow out from water inlet pipe 6.
In addition, above-mentioned rising pipe 7 is provided with regenerated liquid water inlet pipe 8 at its tube wall during as back flushing water inlet pipe, and the sidewall of tank body 1 is provided with regenerated liquid rising pipe 9, and regenerated liquid rising pipe 9 setting adjacent with water inlet pipe 6, and the bottom of tank body 1 is provided with back flushing water inlet pipe 10.
In addition, the sidewall of above-mentioned back flushing water inlet pipe 10 is also provided with the discharge tube 11 for emptying resin.
In the present embodiment, the sidewall on above-mentioned tank body 1 top is also provided with easy access and changes the upper hand-hole 12 of water cap 5.The sidewall on above-mentioned tank body 1 top is also provided with the inspection window 13 for loaded resin and observation inner case.
In the present embodiment, in above-mentioned tank body 1, be also provided with the filter plate support 14 for supporting filter plate 4.The bottom of above-mentioned tank body 1 is also provided with the load-bearing foot rest 15 for supporting tank body 1.
In addition, the outside of above-mentioned tank body 1 is also provided with the cat ladder 16 of being convenient to enter hand-hole 12.
Principle of work of the present utility model is as follows:
1) while normally operation former water from water inlet pipe 6 through water cap 5, filter plate 4 enter ion exchange resin 3 sheaf space, water inlet is first to press down the rising of turning back again in the mistake stream mode of ion exchange resin 3, and former water flows out tank body 1 through water cap 5, filter plate 4 and rising pipe 7 after flowing through resin layer again.
2) the saturated rear back flushing of first carrying out of resin, to clean the suspended substance of water-in one side upper strata resin cut-off filter, back flushing feed water flow to former water feed water flow to contrary, from rising pipe flow into tank body, flow out from water inlet pipe.
3) after back flushing, can carry out resin regeneration, stream of regenerant water, to contrary with former current direction, enters tank body from regenerated liquid water inlet pipe 8, from regenerated liquid rising pipe 9 flows out, enters regeneration waste liquid hold-up vessel.
4) after regeneration, carry out a backwash, to wash away residual regeneration waste liquid, back-flushing flows into tank body from water outlet, flows out from water inlet pipe again.After having recoiled, can normally move, enter next water cycle processed.
5) after some cycles of operation, step 2 can change bottom back flushing into, with the suspended substance of thorough eluted resin surface deposition and cut-off filter, prevents that resin layer from hardening.Back-flushing enters from bottom back flushing water inlet pipe 10, successively opens the set valve of water inlet pipe and rising pipe, to clean the resin layer of separating both sides.
Claims (9)
1. a high-efficiency ion exchanger, it is characterized in that including tank body, vertical partition plate, ion exchange resin, filter plate, water cap, water inlet pipe, rising pipe, tank body is separated into two portions by vertical partition plate, filter plate is installed in the hollow cavity of tank body, water cap is installed on filter plate, ion exchange resin is installed in the hollow cavity of tank body, and be positioned at the below of filter plate, the top of tank body is respectively equipped with water inlet pipe and rising pipe in the both sides of vertical partition plate, when normal operation former water from water inlet pipe through water cap, filter plate enters the upper sheaf space of ion exchange resin, water inlet is first to press down the rising of turning back again in the mistake stream mode of ion exchange resin, former water flows through after ion exchange resin again through water cap, filter plate and rising pipe flow out tank body.
2. high-efficiency ion exchanger according to claim 1, it is characterized in that above-mentioned water inlet pipe in the time of back flushing as back flushing rising pipe, rising pipe in when recoil as back flushing water inlet pipe, back flushing feed water flow to former water feed water flow to contrary, flow into tank body from rising pipe, flow out from water inlet pipe.
3. high-efficiency ion exchanger according to claim 2, while it is characterized in that above-mentioned rising pipe as back flushing water inlet pipe, be provided with regenerated liquid water inlet pipe at its tube wall, the sidewall of tank body is provided with regenerated liquid rising pipe, and the adjacent setting of regenerated liquid rising pipe and water inlet pipe, the bottom of tank body is provided with back flushing water inlet pipe.
4. high-efficiency ion exchanger according to claim 3, is characterized in that the sidewall of above-mentioned back flushing water inlet pipe is also provided with the discharge tube for emptying resin.
5. according to the high-efficiency ion exchanger described in claim 1 to 4 any one, it is characterized in that the sidewall on above-mentioned tank body top is also provided with the upper hand-hole of easy access and replacing water cap.
6. high-efficiency ion exchanger according to claim 5, is characterized in that the sidewall on above-mentioned tank body top is also provided with the inspection window for loaded resin and observation inner case.
7. high-efficiency ion exchanger according to claim 5, is characterized in that being also provided with in above-mentioned tank body the filter plate support for supporting filter plate.
8. high-efficiency ion exchanger according to claim 5, is characterized in that the bottom of above-mentioned tank body is also provided with the load-bearing foot rest of supporting tank body.
9. high-efficiency ion exchanger according to claim 5, is characterized in that the outside of above-mentioned tank body is also provided with the cat ladder of being convenient to enter hand-hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420064528.0U CN203700077U (en) | 2014-02-13 | 2014-02-13 | Efficient ion exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420064528.0U CN203700077U (en) | 2014-02-13 | 2014-02-13 | Efficient ion exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203700077U true CN203700077U (en) | 2014-07-09 |
Family
ID=51050544
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420064528.0U Expired - Lifetime CN203700077U (en) | 2014-02-13 | 2014-02-13 | Efficient ion exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203700077U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104925998A (en) * | 2015-06-29 | 2015-09-23 | 西安华广电站锅炉有限公司 | Multifunctional return-stroke-type water treater |
| CN105016427A (en) * | 2015-07-01 | 2015-11-04 | 太仓市顺邦防腐设备有限公司 | Water softening ion exchanger |
| CN105645515A (en) * | 2016-03-24 | 2016-06-08 | 太仓运权化工防腐设备有限公司 | Hard water softening exchanger device |
| CN107224998A (en) * | 2017-06-23 | 2017-10-03 | 成都虹波钼业有限责任公司 | A kind of ion exchange column screen mesh type water cap |
| CN108779004A (en) * | 2016-03-18 | 2018-11-09 | 栗田工业株式会社 | Ion interchange unit and its application method |
-
2014
- 2014-02-13 CN CN201420064528.0U patent/CN203700077U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104925998A (en) * | 2015-06-29 | 2015-09-23 | 西安华广电站锅炉有限公司 | Multifunctional return-stroke-type water treater |
| CN105016427A (en) * | 2015-07-01 | 2015-11-04 | 太仓市顺邦防腐设备有限公司 | Water softening ion exchanger |
| CN108779004A (en) * | 2016-03-18 | 2018-11-09 | 栗田工业株式会社 | Ion interchange unit and its application method |
| CN105645515A (en) * | 2016-03-24 | 2016-06-08 | 太仓运权化工防腐设备有限公司 | Hard water softening exchanger device |
| CN107224998A (en) * | 2017-06-23 | 2017-10-03 | 成都虹波钼业有限责任公司 | A kind of ion exchange column screen mesh type water cap |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140709 |