CN203284229U - Double-chamber and double-layer room bed compound ion exchanger - Google Patents
Double-chamber and double-layer room bed compound ion exchanger Download PDFInfo
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- CN203284229U CN203284229U CN2013203191590U CN201320319159U CN203284229U CN 203284229 U CN203284229 U CN 203284229U CN 2013203191590 U CN2013203191590 U CN 2013203191590U CN 201320319159 U CN201320319159 U CN 201320319159U CN 203284229 U CN203284229 U CN 203284229U
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- ion exchanger
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Abstract
The utility model discloses a double-chamber and double-layer room bed compound ion exchanger which comprises an ion exchanger body (1). The double-chamber and double-layer room bed compound ion exchanger is characterized in that a three-layer perforated plate (2) is connected to the wall of an inner cavity of the ion exchanger body (1) and divides the inner cavity of the ion exchanger body (1) into two chambers which are arranged in the vertical direction. The inner cavity of the ion exchanger is divided into the upper chamber and the lower chamber, strong resin is arranged in one of the chambers, weak resin is arranged in the other chamber, the problem of layer mixing of the resin is solved, and special requirements for the density and the particle size of the resin do not exist. Meanwhile, the double-chamber and double-layer room bed compound ion exchanger has the advantages that the effluent quality is high, regeneration specific consumption is low, the flow speed is high, the output force of the ion exchanger is large, and the phenomena of bias current and penetration do not exist. The water consumption of the ion exchanger is low, the emission of waste liquid is little, and pollution to the environment is reduced.
Description
Technical field
The utility model relates to mechanical manufacturing field, relates in particular to the ion exchanger in brine treatment technique.
Background technology
Ion exchanger claims again water softener, softening water, ion-exchange.The exchange resin layering is seated in same interchanger, forms the form of double bunk.Although strong and weak resin can be accomplished layering substantially due to the difference of density, accomplish that complete layering is very difficult.If the intersection at two kinds of resins has a small amount of resin-phase to mix, operating performance do not had large impact; If mixed fat scope is large, the Weak Type Resin of sneaking in the strong type resin layer can not be brought into play exchange interaction, and the strong type resin of sneaking in Weak Type Resin can not get regeneration, and operating performance is descended greatly.The full chamber ion-exchanger of said structure, exist that the regeneration specific consumption is high, effluent quality is poor, tight and be prone to and penetrate Biased flow phenomenon to the influent quality requirement.
The utility model content
The purpose of this utility model is to overcome the problem that aforesaid device brings, and provides a kind of double chambers and double layer full chamber bed compound ion exchanger.
The technical solution adopted in the utility model is: the compound ion exchanger of double chambers and double layer full chamber bed, comprise the ion exchanger body, be connected with three layers of porous plate on described ion exchanger chamber body wall, described three layers of porous plate are divided into the ion exchanger chamber body two chambers of vertically arranging; Ion exchanger is separated into upper and lower two Room, and strong and weak resin is a Room everywhere.
As further improvement of the utility model, described porous plate is the porous plate with double end water cap; Described ion exchanger body exterior is provided with washing unit.
The beneficial effect that the utility model adopts is: the ion exchanger of this structure is divided into upper and lower two Room with inner chamber, and strong and weak resin is a Room everywhere, has avoided a problem of bringing because of the mixed layer of resin, and density and the granularity of resin do not had particular requirement yet.The result of sieving due to waterpower simultaneously, make the less resin of particle be arranged in bed top, the resin that particle is larger is arranged in the bed bottom, at first the water of access arrangement contact the large resin of particle, make bed resistance less, therefore pressure reduction is steady, and the improved result of its hydraulic performance moves that flow velocity is high, equipment is exerted oneself greatly, effluent quality is good.The when regeneration acid of this equipment, alkali specific consumption are very low, and the water yield of therefore cleaning spent acid, alkali is also along with minimizing, and the acid of discharging from system, alkali waste water total amount also just reduce, and concentration is also low, this has not only saved the soda acid amount, has also reduced the self water consumption of system, has saved valuable water resources.Because the water of discharging approaches neutrality, the processing of acid-base waste fluid also becomes and is easy to, thereby has reduced cost of sewage disposal, has alleviated the pollution of useless acid base pair environment.In addition, when being tending towards forming, equipment penetrates and when bias current occurred, the partial water Flow Velocity will be too high, resin around this moment will be poured into bias current place with current and fill up this part zone, make bed be tending towards smooth, thereby avoided penetrating, the generation of bias current, guaranteed the effluent quality of interchanger.
Description of drawings
Fig. 1 is the utility model schematic diagram.
Shown in figure: 1 ion exchanger body, 2 porous plates, 3 double end water caps.
Embodiment
Below in conjunction with Fig. 1, the utility model is described further.
As shown in Figure 1, the compound ion exchanger of double chambers and double layer full chamber bed, comprise ion exchanger body 1, be connected with three layers of porous plate 2 on described ion exchanger body 1 internal chamber wall, three layers of porous plate 2 are divided into ion exchanger body 1 inner chamber two chambers of vertically arranging, little and the inert plastic that particle is large of tamped density in two chambers.
Ion exchanger is separated into upper and lower two Room, and strong and weak resin is a Room everywhere,, with regard to having avoided the problem of bringing because of the mixed layer of resin, simultaneously density and the granularity of resin is not had particular requirement yet like this.Chamber interior is filled full ion exchange resin and inert plastic, wherein goes up chamber and fills strong ion exchange resin (sun/the moon), and weak ion exchange resin (sun/the moon) is filled in lower chamber, and the resin yin and yang attribute of upper and lower chamber is consistent.Porous plate 2 with double end water cap 3 is housed, to link up the current between two Room between two Room, up and down.In order to prevent that resin from passing through the gap of water cap or obstruction water cap, the inert plastic of the top filling floating bed special use of resin layer, its pack height is generally 200 mm.Use the equipment of this structure owing to filling resin in chamber,, so can not clean in vivo, need separately establish external washing unit.
Claims (3)
1. the compound ion exchanger of double chambers and double layer full chamber bed, comprise ion exchanger body (1), it is characterized in that being connected with three layers of porous plate (2) on described ion exchanger body (1) internal chamber wall, described three layers of porous plate (2) are divided into ion exchanger body (1) inner chamber two chambers of vertically arranging.
2. the compound ion exchanger of double chambers and double layer full chamber bed according to claim 1, is characterized in that described porous plate (2) is the porous plate with double end water cap (3).
3. the compound ion exchanger of double chambers and double layer full chamber bed according to claim 1 and 2, is characterized in that described ion exchanger body (1) outside is provided with washing unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203191590U CN203284229U (en) | 2013-06-05 | 2013-06-05 | Double-chamber and double-layer room bed compound ion exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203191590U CN203284229U (en) | 2013-06-05 | 2013-06-05 | Double-chamber and double-layer room bed compound ion exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203284229U true CN203284229U (en) | 2013-11-13 |
Family
ID=49540603
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013203191590U Expired - Fee Related CN203284229U (en) | 2013-06-05 | 2013-06-05 | Double-chamber and double-layer room bed compound ion exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203284229U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439244A (en) * | 2016-01-06 | 2016-03-30 | 上海振世能源科技有限公司 | Ion exchange resin desalting device |
-
2013
- 2013-06-05 CN CN2013203191590U patent/CN203284229U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105439244A (en) * | 2016-01-06 | 2016-03-30 | 上海振世能源科技有限公司 | Ion exchange resin desalting device |
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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: 20131113 Termination date: 20180605 |