CN2285159Y - Double-chamber float ion exchanger - Google Patents
Double-chamber float ion exchanger Download PDFInfo
- Publication number
- CN2285159Y CN2285159Y CN96248194U CN96248194U CN2285159Y CN 2285159 Y CN2285159 Y CN 2285159Y CN 96248194 U CN96248194 U CN 96248194U CN 96248194 U CN96248194 U CN 96248194U CN 2285159 Y CN2285159 Y CN 2285159Y
- Authority
- CN
- China
- Prior art keywords
- resin
- pipe
- utility
- model
- tank body
- 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
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- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a double working chamber water treatment equipment for exchanging ionized water. The utility model is composed of a tank body, a water inlet pipe, an actified solution pipe and a drainage pipe, wherein, three payers of partition boards arranged in the tank divide the tank body into two chambers, and resin of weak character, inert resin, resin of strong character are respectively filled in the two chambers; during the running of the utility model, the resin are in a boiling state, the drainage pipe is in the shape of an inverted U, and an inward arrangement type device for withdrawing a sample is installed in the drainage pipe. The utility model has the advantages that running resistance is small, flow speed is fast and can reach 30 meters to 50 meters per hour, ability in processing water is high, the quality of discharged water is favorable, and the consumption volume of actified solution is small; besides, drainage quantity is less, running cost is low, a sample is sampled in time, the utility model is easy to operate, etc.
Description
The utility model relates to a kind of ion exchange water treatment equipment, particularly with the ion exchange water treatment equipment of two operating rooms.
The ion-exchange unit that is used for water treatment, more advanced have bunk beds, floating bed etc., but have to resin requirement condition harshness, strong and weak resin mixes layer easily.Whether qualified sampler is installed on the outlet pipe water outlet of general mensuration ion-exchanger, work lagging influence effluent characteristics.Sewage is directly discharged downwards from the blow-off pipe of interchanger bottom, makes air enter resin bed easily and makes the resin can't operate as normal.
It is good that the purpose of this utility model just provides a kind of effluent quality, and sour alkali consumes low, and the not random layer of resin can avoid air to enter resin bed again during blowdown, can in time carry out the novel ion exchange water treatment equipment of effluent quality sampling.
The purpose of this utility model realizes by following manner, three floor dividing plate are housed in tank body tank body is divided into two big chambers up and down, weak acid (alkali) property ion exchange resin is filled by down indoor lower floor, inert plastic is filled on the upper strata, fill strong acid (alkali) property ion exchange resin in last indoor lower floor, inert plastic is filled on the upper strata, in last chamber strong acid (alkali) property resin bed middle and upper part sampler is housed, and the blow-off pipe that is positioned at tank base is inverted U-shaped.
The utility model up and down two is indoorly being filled strong, weak property ion exchange resin respectively, processed water is earlier through behind the weak property resin, twice exchange can be increased water quality through the epistasis resin again, inert plastic is all filled on resin top, two Room, because little material of its proportion floats on each top, chamber greatly automatically, can prevent that thereby broken resin from stopping up the water cap and can reduce running resistance, regenerative agent is earlier through strong acid (alkali) property ion exchange resin during regeneration, pass through weak acid (alkali) property resin again, regenerated liquid is fully used.The sampler that is positioned at chamber strong acid (alkali) property sun (the moon) resinbed can early detect the resin out-of-service time, in time stops interchanger and outwards supplies water, thereby guaranteed water supply quality.Be inverted U-shaped blow-off pipe and can prevent that air enters resin bed and influences the resins exchange performance when blowdown.
The concrete structure of utility model is provided by following examples and accompanying drawing thereof.
Fig. 1 is a structural representation of the present utility model.
Below, in conjunction with the accompanying drawings the utility model is further specified.
By tank body (2), water inlet pipe (1), outlet pipe (11), regenerated liquid pipe (10), blow-off pipe (13), the ion-exchange unit that resin bed is formed, three layers of dividing plate (3) are arranged in the tank body, (6), (9), tank body is divided into two big chambers, following indoor under-filled weak acid (alkali) property sun (the moon) ion exchange resin (4), inert plastic (5) is filled on top, go up indoor under-filled strong acid (alkali) property sun (the moon) ion exchange resin (7), inert plastic (8) is filled on top, in last chamber strong acid (alkali) property sun (the moon) ion exchange resin floor, sampler (14) is housed, the blow-off pipe (13) that is positioned at tank base is inverted U-shaped, its the highest portion is higher than tank body and pipeline, and the top is provided with emptying valve (12).
The dividing plate of ion-exchanger can be made up of folder filter cloth between the two porous plates, also water filtering cap (15) can be installed on porous plate.
Processed water enters interchanger by water inlet pipe and at first flows through the weak acid resin layer with removing firmly temporarily in the water during operation, and then through inert plastic, the last chamber of dividing plate inflow strong resin floor, hard temporarily and other cations of the fraction that the weakly acidic resin layer is leaked are removed, and the anion exchanger working condition is also same.Processed water makes resin in indoor formation quick condition in the process of flowing in interchanger from bottom to top, because it is little that inert plastic is filled in its proportion of top, every chamber, can play barrier resin contact water filtering cap above always floating over and prevent that broken resin from stopping up the water cap, thereby play the effect that reduces running resistance.
Claims (3)
1. by tank body (2), water inlet pipe (1), outlet pipe (11), regenerated liquid pipe (10), blow-off pipe (13), the ion exchange water treatment equipment that resin bed is formed, it is characterized in that having in the tank body three layers of dividing plate (3), (6), (9), tank body is divided into two chambers, weak acid (alkali) property ion exchange resin (4) is filled by down indoor lower floor, inert plastic (5) is filled on the upper strata, go up indoor lower floor and fill strong acid (alkali) property ion exchange resin (7), inert plastic (8) is filled on the upper strata, in last chamber strong acid (alkali) property resin bed inside sampler (14) is housed, the blow-off pipe (13) that is positioned at tank base is inverted U-shaped.
2. ion-exchange unit according to claim 1 is characterized in that its most significant end of inverted U-shaped blow-off pipe is higher than tank body and pipeline, and the top is provided with emptying valve (12).
3. ion-exchange unit according to claim 1, it is characterized in that dividing plate can by between the two porous plates folder filter cloth form, also water filtering cap (15) can be installed on porous plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96248194U CN2285159Y (en) | 1996-11-05 | 1996-11-05 | Double-chamber float ion exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96248194U CN2285159Y (en) | 1996-11-05 | 1996-11-05 | Double-chamber float ion exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2285159Y true CN2285159Y (en) | 1998-07-01 |
Family
ID=33920120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96248194U Expired - Fee Related CN2285159Y (en) | 1996-11-05 | 1996-11-05 | Double-chamber float ion exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2285159Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104724791A (en) * | 2014-12-11 | 2015-06-24 | 中机国能电力工程有限公司 | Method for normally operating double-chamber double-layer floating bed under any heat supply working condition |
| CN106076440A (en) * | 2016-06-14 | 2016-11-09 | 云南文山铝业有限公司 | Ion exchanger |
-
1996
- 1996-11-05 CN CN96248194U patent/CN2285159Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104724791A (en) * | 2014-12-11 | 2015-06-24 | 中机国能电力工程有限公司 | Method for normally operating double-chamber double-layer floating bed under any heat supply working condition |
| CN106076440A (en) * | 2016-06-14 | 2016-11-09 | 云南文山铝业有限公司 | Ion exchanger |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |