CN206368057U - A kind of electric osmose chemical reaction water treatment facilities - Google Patents
A kind of electric osmose chemical reaction water treatment facilities Download PDFInfo
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- CN206368057U CN206368057U CN201621409942.6U CN201621409942U CN206368057U CN 206368057 U CN206368057 U CN 206368057U CN 201621409942 U CN201621409942 U CN 201621409942U CN 206368057 U CN206368057 U CN 206368057U
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- exchange membrane
- river
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- anion
- water
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Abstract
The utility model is related to a kind of electric osmose chemical reaction water treatment facilities, including water inlet 1, produce the mouth of a river 2, the alkaline aquatic products mouth of a river 3, the acid aquatic products mouth of a river 4, minus plate 5, positive plate 6, cation-exchange membrane 7, anion-exchange membrane 8, dc source 9, wherein, there are a pair of anion and cation exchange membranes between each pair cathode-anode plate, all cation-exchange membranes 7 are close to minus plate 5, all anion-exchange membranes 8 are close to positive plate 6, three strands of aquaporins are formed between each pair pole plate, alkaline aquaporin is formed i.e. between cation-exchange membrane 7 and minus plate 5, acid aquaporin is formed between anion-exchange membrane 8 and positive plate 6, production aquaporin is formed between cation-exchange membrane 7 and anion-exchange membrane 8.During work, zwitterion is enriched with through amberplex anisotropy battery lead plate in the presence of electric field force and occurs cell reaction, so as to reduce the ion concentration of production water, and produces alkaline water and acid water, reaches water process purpose.
Description
Technical field
The utility model belongs to water-treatment technology field, is specifically related to a kind of electric osmose chemical reaction water treatment facilities.
Background technology
Electrodialysis（Abbreviation ED）Water technology is the technology of a comparative maturity, on the basis of ED, with reference to conventional hybrid
Ion-exchange demineralization technique（DI）, generate electronics mixed bed（EDI）Desalination technology, improves desalting efficiency, but EDI is to water inlet water
Matter requires very strict, therefore processing cost is higher.Relative to EDI, and then derive EDR technologies, one kind utilizes ion exchange
Film is to the selective penetrated property of zwitterion in solution, using DC electric field as the membrane separating method of motive force.It is all to have with electrodialysis
The water technology of pass finally can all have strong brine generation, and the processing for these strong brines turns into a problem again.
Chemically reacted the utility model proposes a kind of method for treating water of new electrodialysis combination cell reaction, i.e. electric osmose
（EDER）A pair of cathode-anode plates on the basis of traditional EDR, are become multipair by method for treating water, and one is included between each pair pole plate
To anion and cation exchange membrane, the zwitterion that can thus will transmit through anion and cation exchange membrane is separated out, and occurs cell reaction,
Deionized water is not only generated, alkaline water and acid water is also formed, alkaline water and acid water have its respective application field again, so that
Solve strong brine process problem.
The content of the invention
The problem of the utility model has strong brine generation for the existing water technology relevant with electrodialysis, and
A kind of new water treatment facilities is proposed on the basis of EDR, in addition to producing deionized water, alkaline water and acid water substitution is also produced
Strong brine.The utility model reaches above-mentioned purpose by the following technical programs：
A kind of electric osmose chemical reaction water treatment facilities, including water inlet 1, the production mouth of a river 2, the alkaline aquatic products mouth of a river 3, acid aquatic products
The mouth of a river 4, minus plate 5 and positive plate 6, wherein, the minus plate 5 and positive plate 6 are at least respectively equipped with two groups, the minus plate
5 and positive plate 6 be arranged alternately, one group of cation-exchange membrane 7 and one group are equipped between adjacent minus plate 5 and positive plate 6 cloudy
Amberplex 8.
The further technical scheme of the utility model also includes：
All cation-exchange membranes 7 are close to the side of minus plate 5, and all anion-exchange membranes 8 are close to the side of positive plate 6.
All minus plates 5 are connected with the negative pole of dc source 9, and all positive plates 6 are connected with the positive pole of dc source 9.
Alkaline aquaporin, the anion-exchange membrane 8 and anode are formed between the cation-exchange membrane 7 and minus plate 5
Acid aquaporin is formed between plate 6, production aquaporin is formed between the cation-exchange membrane 7 and anion-exchange membrane 8.
The alkaline aquaporin connects water inlet 1 with the alkaline aquatic products mouth of a river 3, and the acid aquaporin is by the He of water inlet 1
The acid aquatic products mouth of a river 4 is connected, and the production aquaporin connects water inlet 1 with the production mouth of a river 2.
The water inlet 1 is located at the side of electrodialytic water processing unit, the alkaline aquatic products mouth of a river 3, the production mouth of a river 2 and acid
Property the aquatic products mouth of a river 4 be located at electrodialytic water processing unit opposite side.
Compared with prior art, advantageous effects of the present utility model are：Through anion and cation exchange membrane negative and positive from
Son is separated out, and not only generates deionized water, and the alkaline water and acid water of generation instead of strong brine, and alkaline water and acid water
There is its respective application field again, so as to solve strong brine process problem.
Brief description of the drawings
Fig. 1 is a kind of theory structure schematic diagram of electric osmose chemical reaction water treatment facilities of the utility model；
Wherein：
1st, water inlet 2, the production mouth of a river 3, the alkaline aquatic products mouth of a river
4th, the acid aquatic products mouth of a river 5, minus plate 6, positive plate
7th, cation-exchange membrane 8, anion-exchange membrane 9, dc source
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is further described.
Referring to Fig. 1, a kind of electric osmose chemical reaction water treatment facilities of the utility model, including water inlet 1, the production mouth of a river 2, alkali
Property the aquatic products mouth of a river 3, the acid aquatic products mouth of a river 4, minus plate 5 and positive plate 6, wherein, at least two groups of minus plate 5, positive plate 6
At least two groups, minus plate 5 and positive plate 6 are arranged alternately, i.e., one group minus plate 5, one group of positive plate 6；Another group minus plate 5,
One group of positive plate 6 ..., the rest may be inferred, is equipped with one group of He of cation-exchange membrane 7 between adjacent minus plate 5 and positive plate 6
There are a pair of anion and cation exchange membranes between one group of anion-exchange membrane 8, i.e. each pair cathode-anode plate；All cation-exchange membranes 7
Close to the side of minus plate 5, all anion-exchange membranes 8 are just formed between the side of positive plate 6, so every a pair of cathode-anode plates
Between passage, anion-exchange membrane 8 and positive plate 6 between three strands of aquaporins, i.e. cation-exchange membrane 7 and minus plate 5 with
And the passage between cation-exchange membrane 7 and anion-exchange membrane 8.All minus plates 5 are connected with the negative pole of dc source 9, institute
There are positive plate 6 and the positive pole of dc source 9 to be connected.
In the embodiment of the utility model one, the passage between cation-exchange membrane 7 and minus plate 5 is alkaline aquaporin, the moon
Passage between amberplex 8 and positive plate 6 is acid aquaporin, between cation-exchange membrane 7 and anion-exchange membrane 8
Passage is production aquaporin；Alkaline aquaporin connects water inlet 1 with the alkaline aquatic products mouth of a river 3, and acid aquaporin is by water inlet 1 and acid
Property the aquatic products mouth of a river 4 connect, production aquaporin by water inlet 1 and produce the mouth of a river 2 connect；Water inlet 1 is located at electrodialytic water processing unit
Side, the alkaline aquatic products mouth of a river 3, the production mouth of a river 2 and the acid aquatic products mouth of a river 4 are located at the opposite side of electrodialytic water processing unit.
After dc source 9 is connected, the water containing electrolyte simultaneously by all passages when, under the driving of electric field force,
Cation will be enriched with through cation-exchange membrane 7 to minus plate 5, and anion will pass through anion-exchange membrane 8 to positive plate 6
Enrichment, and discharged respectively in pole plate and occur cell reaction.Water so between cation-exchange membrane 7 and anion-exchange membrane 8
Zwitterion will be lost, deionized water is generated.Water between minus plate 5 and cation-exchange membrane 7 obtains cation and occurred
Catholyte reacts, and generates alkaline water.Water between positive plate 6 and anion-exchange membrane 8 obtains the concurrent green anode electricity of anion
Solution reaction, generates acid water.Then the passage between minus plate 5 and cation-exchange membrane 7 is formed alkaline aquaporin, anode
Passage between plate 6 and anion-exchange membrane 8 is formed acid aquaporin, cation-exchange membrane 7 and anion-exchange membrane 8 it
Between passage be formed produce aquaporin.
Following steps can be substantially divided into by carrying out water process using the utility model electric osmose chemical reaction water treatment facilities：
Water inlet, accessing pending water imports electrodialytic water processing unit by water inlet 1；
Shunting, the accessing pending water imported in electrodialytic water processing unit is divided into three strands：One flows through alkaline aquaporin, one
Plume is through producing aquaporin, and one flows through acid aquaporin；
Cation permeable cation-exchange membrane 7 in separation, accessing pending water is moved to the side direction of minus plate 5, is occurred cloudy
Pole cell reaction, generates alkaline water；Anion-permeable anion-exchange membrane 8 in accessing pending water is moved to the side direction of positive plate 9
It is dynamic, occur anode electrolysis reaction, generate acid water；Water between cation-exchange membrane 7 and anion-exchange membrane 8 lose negative and positive from
Son, generates deionized water；
Water outlet, the alkaline water isolated is exported via alkaline aquaporin from the alkaline aquatic products mouth of a river 3, and acid water is via acid water
Passage is exported from the acid aquatic products mouth of a river 4, and deionized water is exported via production aquaporin from the production mouth of a river 2.
Separated out through the zwitterion of anion and cation exchange membrane, not only generate deionized water, the alkaline water of generation and
Acid water instead of strong brine, and alkaline water and acid water have its respective application field, so as to solve strong brine processing
Problem, has thus reached water process purpose.
Preferred embodiment of the present utility model is these are only, not to limit the utility model.It is all in the utility model
Principle within any modifications, equivalent substitutions and improvements for being made etc., should be included within protection domain of the present utility model.
Claims (6)
- The water treatment facilities 1. a kind of electric osmose chemically reacts, including water inlet（1）, production the mouth of a river（2）, the alkaline aquatic products mouth of a river（3）, it is acid The aquatic products mouth of a river（4）, minus plate（5）And positive plate（6）, it is characterised in that the minus plate（5）And positive plate（6）At least divide She You not be two groups, the minus plate（5）And positive plate（6）It is arranged alternately, adjacent minus plate（5）And positive plate（6）Between Provided with one group of cation-exchange membrane（7）With one group of anion-exchange membrane（8）.
- 2. a kind of electric osmose chemical reaction water treatment facilities according to claim 1, it is characterised in that all cation exchanges Film（7）Close to minus plate（5）Side, all anion-exchange membranes（8）Close to positive plate（6）Side.
- 3. a kind of electric osmose chemical reaction water treatment facilities according to claim 1, it is characterised in that all minus plates（5） With dc source（9）Negative pole connection, all positive plates（6）With dc source（9）Positive pole connection.
- 4. a kind of electric osmose chemical reaction water treatment facilities according to claim 1 or 2, it is characterised in that the cation Exchange membrane（7）With minus plate（5）Between form alkaline aquaporin, the anion-exchange membrane（8）With positive plate（6）Between formed Acid aquaporin, the cation-exchange membrane（7）With anion-exchange membrane（8）Between formed production aquaporin.
- 5. a kind of electric osmose chemical reaction water treatment facilities according to claim 4, it is characterised in that the alkaline aquaporin By water inlet（1）With the alkaline aquatic products mouth of a river（3）Connection, the acid aquaporin is by water inlet（1）With the acid aquatic products mouth of a river（4）Even Logical, the aquaporin that produces is by water inlet（1）With the production mouth of a river（2）Connection.
- 6. a kind of electric osmose chemical reaction water treatment facilities according to claim 5, it is characterised in that the water inlet（1） Positioned at the side of electrodialytic water processing unit, the alkaline aquatic products mouth of a river（3）, production the mouth of a river（2）And the acid aquatic products mouth of a river（4）Position In the opposite side of electrodialytic water processing unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621409942.6U CN206368057U (en) | 2016-12-21 | 2016-12-21 | A kind of electric osmose chemical reaction water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621409942.6U CN206368057U (en) | 2016-12-21 | 2016-12-21 | A kind of electric osmose chemical reaction water treatment facilities |
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| Publication Number | Publication Date |
|---|---|
| CN206368057U true CN206368057U (en) | 2017-08-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621409942.6U Expired - Fee Related CN206368057U (en) | 2016-12-21 | 2016-12-21 | A kind of electric osmose chemical reaction water treatment facilities |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106477687A (en) * | 2016-12-21 | 2017-03-08 | 新疆融通利和水处理技术有限公司 | A kind of electric osmose chemical reaction water treatment facilities and method |
-
2016
- 2016-12-21 CN CN201621409942.6U patent/CN206368057U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106477687A (en) * | 2016-12-21 | 2017-03-08 | 新疆融通利和水处理技术有限公司 | A kind of electric osmose chemical reaction water treatment facilities and method |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170801 Termination date: 20171221 |