CN206308425U - A kind of utilization Electro Sorb processes the device of brine waste - Google Patents
A kind of utilization Electro Sorb processes the device of brine waste Download PDFInfo
- Publication number
- CN206308425U CN206308425U CN201621152228.3U CN201621152228U CN206308425U CN 206308425 U CN206308425 U CN 206308425U CN 201621152228 U CN201621152228 U CN 201621152228U CN 206308425 U CN206308425 U CN 206308425U
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- CN
- China
- Prior art keywords
- electrolytic cell
- processes
- brine waste
- electro sorb
- connecting bracket
- 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.)
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Abstract
The utility model discloses the device that a kind of utilization Electro Sorb processes brine waste,Including device body,Electrolytic cell,Connecting bracket,Described device body is provided with electrolytic cell,Electrolytic cell is made of aluminum material,Minus plate is provided with the inside of electrolytic cell,Positive plate,In minus plate,Barrier film is provided between positive plate,Electrical control cubicles are provided with the left of electrolytic cell,Electrolyte entrance,Sieves,Leakage fluid dram is provided with the right side of electrolytic cell,Air intake is provided with above electrolytic cell,Content gauge,Connecting bracket,Gas outlet,Voltmeter is installed in connecting bracket,Direct current supply module,Ammeter,Present apparatus simple structure,It is reasonable in design,Can be after powered up,Sodium chloride in saline solution is ionized with water,Discharged with chlorine in minus plate and positive plate generation hydrogen respectively,Remaining hydroxide ion is combined generation NaOH Molecular Adsorption with sodium ion on minus plate and positive plate,Discharged by leakage fluid dram by the waste water after electrolysis.
Description
Technical field
The utility model is related to industrial technical field, and specially a kind of utilization Electro Sorb processes the device of brine waste.
Background technology
It is well known that electrolyte is electrolysed and when gas is produced in anode-side, fluidity (pH) warp of cathode side
Shi Bianhua.Such fluidity change has undesirable effect to the electrolyte on anode periphery and reduces the stability of electrolyte, deposits
In the possibility that the generation efficiency of gas is gradually reduced.
Recorded in patent document 2 in the aseptate electrolytic cell for possessing negative electrode and anode to electrolyte supply direct current
Electric current and be electrolysed, thus produce chlorine dioxide chlorine dioxide manufacture method.Specifically, the method is the electrolysis of 1 liquid type
The chlorine dioxide manufacture method of formula, i.e. in the state of the pH of the electrolyte is made for 4~8 to containing alkali chloride, chlorous acid alkali with
And pH adjusting agent above-mentioned electrolyte supply DC current and be electrolysed, in order to supplement electrolysis in consumed along with electrolysis
Chlorous acid alkali, from outside electrolytic cell to the aqueous solution of electrolyte supply chlorous acid alkali, the chlorine dioxide that will be produced is from electrolyte
Take out.
NaOH usually industrially is produced with electrolytic saltwater, if because chlorion contacts meeting with sodium hydroxide solution
Generation NaCl and NaClO (sodium hypochlorite), industrial hydrogen production sodium oxide molybdena using amberplex (do not allow electronegative chlorion or
Chlorine passes through) isolation chlorion and NaOH.
But in some current waste water liquid in the presence of a large amount of salt while also adulterate substantial amounts of impurity, and electrolytic speed
Not fast enough, remaining waste water can not be discharged in time after electrolysis.
Utility model content
The purpose of this utility model is to provide a kind of left and right sides in electrolytic cell to be equipped with three pieces of minus plates and anodes
Plate, we need the ion of extraction in discharging different ions absorption electrolyte after powered up by two blocks of different plates, are provided with
Three pieces of minus plates and positive plate, can so increase contact area, accelerate electrolytic speed；Method by being electrolysed absorption, can
A kind of utilization Electro Sorb that effectively salt in waste water is extracted processes the device of brine waste, to solve above-mentioned background skill
The problem proposed in art.
To achieve the above object, the utility model provides following technical scheme：One kind processes brine waste using Electro Sorb
Device, including device body, electrolytic cell, connecting bracket, described device body is provided with electrolytic cell, the left side of the electrolytic cell
Lower section is provided with electrical control cubicles, and the upper left side on the outside of the electrolytic cell is provided with electrolyte entrance, and the left side lower section of the electrolytic cell is provided with
Leakage fluid dram, barrier film is provided with the bosom of electrolytic cell, and minus plate is provided with the left of the barrier film, is provided with the right side of the barrier film
Positive plate, is provided with connecting bracket above the electrolytic cell, air intake is provided with the left of the connecting bracket, connecting bracket with
Content gauge is provided between air intake, pressure gauge is provided with the right side of the connecting bracket, the manometric right side is provided with gas outlet.
Preferably, the connecting bracket is provided with direct current supply module, and the side of the direct current supply module is provided with electric current
Table, one voltmeter of two ends parallel connection of the direct current supply module.
Preferably, the mouth end of the electrolyte entrance is provided with filtering plug.
Preferably, the electrolyte entrance, leakage fluid dram and electrolytic cell are structure as a whole.
Preferably, the air intake, gas outlet are welded on the top of electrolytic cell.
Preferably, one end connection minus plate of the direct current supply module, one end connection sun of the direct current supply module
Pole plate, minus plate, positive plate are equipped with three pieces in the electrolytic cell.
Preferably, the direct current supply module provides the DC voltage of 220V-320V.
Preferably, the air intake, gas outlet use right angle arc-shaped pipeline.
Preferably, the electrolyte can be flowed by barrier film.
Compared with prior art, the beneficial effects of the utility model are：
(1) barrier film is provided with the centre of electrolytic cell, water can while barrier film can intercept the circulation of specified ion after being electrolysed
Automatic circulation；
(2) three pieces of minus plates and positive plate are equipped with the left and right sides of electrolytic cell, are being powered by two blocks of different plates
We need the ion of extraction in discharging different ions absorption electrolyte afterwards, are provided with three pieces of minus plates and positive plate, such energy
Enough increase contact area, accelerate electrolytic speed；Method by being electrolysed absorption, effectively can extract the salt in waste water
Come；
(3) sieves is provided with electrolyte entrance, the impurity in waste water is kept off in the outside of electrolytic cell, prevent impurity from entering
Enter electrolytic cell.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure：1st, minus plate；2nd, air intake；3rd, content gauge；4th, voltmeter；5th, direct current supply module；6th, ammeter；7th, press
Power table；8th, gas outlet；9th, barrier film；10th, electrolyte entrance；11st, positive plate；12nd, leakage fluid dram；13rd, connecting bracket；14th, electrical control cubicles；
15th, device body；16th, electrolytic cell；17th, sieves.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
Fig. 1 is referred to, the utility model provides a kind of technical scheme：A kind of utilization Electro Sorb processes the dress of brine waste
Put, including device body 15, electrolytic cell 16, connecting bracket 13, device body 15 is provided with electrolytic cell 16, the left side of electrolytic cell 16
Lower section is provided with electrical control cubicles 14, and the upper left side in the outside of electrolytic cell 16 is provided with electrolyte entrance 10, is set at the mouth end of electrolyte entrance 10
There is filtering plug 17, the impurity in waste water is kept off in the outside of electrolytic cell 16, prevent impurity from entering electrolytic cell 16.
The left side lower section of electrolytic cell 16 is provided with leakage fluid dram 12, and electrolyte entrance 10, leakage fluid dram 12 are integrated with electrolytic cell 16
Structure, barrier film 9 is provided with the bosom of electrolytic cell 16, and electrolyte can be flowed by barrier film 9, and barrier film 9 can intercept electrolysis
Water can automatic circulation while specifying the circulation of ion afterwards；The left side of barrier film 9 is provided with minus plate 1, and the right side of barrier film 9 is provided with anode
Plate 11, the top of electrolytic cell 16 is provided with connecting bracket 13, and the left side of connecting bracket 13 is provided with air intake 2, connecting bracket 13 with
Content gauge 3 is provided between air intake 2, the right side of connecting bracket 13 is provided with pressure gauge 7, and the right side of pressure gauge 7 is provided with gas outlet 8,
Air intake 2, gas outlet 8 use right angle arc-shaped pipeline, and air intake 2, gas outlet 8 are welded on the top of electrolytic cell 16.
Connecting bracket 13 is provided with direct current supply module 5, and the side of direct current supply module 5 is provided with ammeter 6, direct current supply
One voltmeter 4 of two ends parallel connection of module 5, one end connection minus plate 1 of direct current supply module 5, one end of direct current supply module 5
Jointed anode plate 11, direct current supply module 5 provides the DC voltage of 220V-320V, minus plate 1, positive plate 11 in electrolytic cell 16
Three pieces are equipped with, can so increase contact area, accelerate electrolytic speed；By be electrolysed absorption method, can effectively by
Salt in waste water is extracted.
Often in chaotic motion, after leading to direct current, the ion in electrolyte makees orientation fortune to ion in electrolyte
Dynamic cation obtains electronics to movable cathode in negative electrode, and Ghandler motion is moved on the sunny side to be reduced anion, and electronics is lost by oxygen in anode
Change.In water electrolysis process, hydroxyl loses electronics in anode, is oxidized to oxygen releasing, and H obtains electronics, gone back in negative electrode
It is former to be released into hydrogen, the ion of corresponding polarity is released to positive plate 11 by minus plate 1, so that the ion that will lack is from electrolyte
In obtain, absorption is electrolysed the product for obtaining on minus plate 1 and positive plate 11 so as to obtain us.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out various changes in the case where principle of the present utility model and spirit is not departed from, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (9)
1. a kind of utilization Electro Sorb processes the device of brine waste, including device body (15), electrolytic cell (16), connecting bracket
(13), it is characterised in that：Described device body (15) is provided with electrolytic cell (16), and the left side lower section of the electrolytic cell (16) is provided with
Electrical control cubicles (14), the upper left side on the outside of the electrolytic cell (16) is provided with electrolyte entrance (10), the left side of the electrolytic cell (16)
Lower section is provided with leakage fluid dram (12), and barrier film (9) is provided with the bosom of electrolytic cell (16), and the moon is provided with the left of the barrier film (9)
Pole plate (1), is provided with positive plate (11) on the right side of the barrier film (9), connecting bracket (13) is provided with above the electrolytic cell (16),
Air intake (2) is provided with the left of the connecting bracket (13), content gauge is provided between connecting bracket (13) and air intake (2)
(3) pressure gauge (7), is provided with the right side of the connecting bracket (13), gas outlet (8) is provided with the right side of the pressure gauge (7).
2. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：The connection
Support (13) is provided with direct current supply module (5), and the side of the direct current supply module (5) is provided with ammeter (6), the direct current
One voltmeter (4) of two ends parallel connection of power supply module (5).
3. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：The electrolysis
The mouth end of liquid entrance (10) is provided with filtering plug (17).
4. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：The electrolysis
Liquid entrance (10), leakage fluid dram (12) are structure as a whole with electrolytic cell (16).
5. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：It is described enter gas
Mouth (2), gas outlet (8) are welded on the top of electrolytic cell (16).
6. a kind of utilization Electro Sorb according to claim 2 processes the device of brine waste, it is characterised in that：The direct current
One end of power supply module (5) connects minus plate (1), one end jointed anode plate (11) of the direct current supply module (5), the electricity
Minus plate (1), positive plate (11) are equipped with three pieces in Xie Chi (16).
7. a kind of utilization Electro Sorb according to claim 2 processes the device of brine waste, it is characterised in that：The direct current
Power supply module (5) provides the DC voltage of 220V-320V.
8. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：It is described enter gas
Mouth (2), gas outlet (8) use right angle arc-shaped pipeline.
9. a kind of utilization Electro Sorb according to claim 1 processes the device of brine waste, it is characterised in that：The electrolysis
Liquid energy is enough flowed by barrier film (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621152228.3U CN206308425U (en) | 2016-10-31 | 2016-10-31 | A kind of utilization Electro Sorb processes the device of brine waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621152228.3U CN206308425U (en) | 2016-10-31 | 2016-10-31 | A kind of utilization Electro Sorb processes the device of brine waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206308425U true CN206308425U (en) | 2017-07-07 |
Family
ID=59242744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621152228.3U Expired - Fee Related CN206308425U (en) | 2016-10-31 | 2016-10-31 | A kind of utilization Electro Sorb processes the device of brine waste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206308425U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108996774A (en) * | 2018-07-23 | 2018-12-14 | 山东龙安泰环保科技有限公司 | A kind of processing method of high hydrochloric acid waste water |
-
2016
- 2016-10-31 CN CN201621152228.3U patent/CN206308425U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108996774A (en) * | 2018-07-23 | 2018-12-14 | 山东龙安泰环保科技有限公司 | A kind of processing method of high hydrochloric acid waste water |
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Legal Events
| 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: 20170707 Termination date: 20171031 |