CN206511967U - A kind of katholysis Heavy metal separation device - Google Patents
A kind of katholysis Heavy metal separation device Download PDFInfo
- Publication number
- CN206511967U CN206511967U CN201621478189.6U CN201621478189U CN206511967U CN 206511967 U CN206511967 U CN 206511967U CN 201621478189 U CN201621478189 U CN 201621478189U CN 206511967 U CN206511967 U CN 206511967U
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- China
- Prior art keywords
- electrolytic cell
- heavy metal
- pipeline
- ion exchange
- katholysis
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Abstract
The utility model discloses a kind of katholysis Heavy metal separation device, including electrolytic cell, electrolytic cell upper end is provided with upper end cover, electrolytic cell inner chamber is provided with amberplex, amberplex both sides are respectively equipped with minus plate and positive plate, upper end cover is provided with negative terminal and positive terminal and inlet opening, negative terminal connects minus plate, positive terminal jointed anode plate, feed tube is fixed with inlet opening, electrolytic cell bottom is provided with leakage fluid dram, discharging tube is fixed with leakage fluid dram, discharging tube connecting detection mechanism, testing agency connects waste liquid recovery apparatus by pipeline, the utility model structural principle is simple, it is easy to operate, quick separating can be carried out to the heavy metal ion in sewage, multi-cycle separation can also be carried out to the sewage of discharge simultaneously, improve disintegrate-quality.
Description
Technical field
The utility model is related to heavy metal isolation technics field, specially a kind of katholysis Heavy metal separation device.
Background technology
Heavy metal wastewater thereby is environmental pollution and the mankind is endangered with one of maximum industrial wastewater, is difficult in the environment by generation
Thank, and repair difficult, very serious harm is caused to natural environment and daily life, for example, Poland is by digging up mine
About 50% surface water is caused not reach water quality grade III Standard with waste is smelted；" the Minamata that Japanese Minamata bay is caused by mercury poisoning
" bone aching " of disease " and remarkable ability river basin caused by cadmium, " blood lead event " that the ground lead contamination such as China Shaanxi Fengxiang is caused, Fujian
Cu-W ore deposit that Zijin Mining seepage accident is caused etc., is all the typical thing that heavy metal pollution brings infringement to health and environment
It is real.
With China's economy, the development of society, shortage of water resources, water pollution problems are on the rise.Relevant statistics shows, I
State's heavy metal wastewater thereby accounts for the 10% of wastewater emission amount, essentially from industry such as plating, wiring board, mining, metallurgy, chemical industry,
There is significant bio-toxicity with potentially hazardous property, the particularly heavy metal such as mercury, cadmium, lead, chromium, micro-concentrations can be produced
Toxicity, can be converted into the stronger organo-metallic compound of toxicity (such as methyl mercury) under microbial action, or be bioaccumulation, and lead to
Cross food chain and enter human body, cause slow poisoning.Existing heavy metal wastewater thereby electrolysis unit is bulky, complicated, exists
Current density is small in electrolytic process, solution removal of impurities difficulty is big, operating process length, production cost are high, under low production efficiency the problems such as.
Utility model content
The purpose of this utility model is to provide a kind of katholysis Heavy metal separation device, to solve above-mentioned background skill
The problem of being proposed in art.
To achieve the above object, the utility model provides following technical scheme：A kind of katholysis heavy metal separation dress
Put, including electrolytic cell, the electrolytic cell upper end is provided with amberplex, the ion provided with upper end cover, the electrolytic cell inner chamber
Exchange membrane both sides are respectively equipped with minus plate and positive plate, the upper end cover provided with negative terminal and positive terminal with
And inlet opening, the negative terminal connects solid in minus plate, the positive terminal jointed anode plate, the inlet opening
Surely feed tube is provided with, the electrolytic cell bottom, which is provided with leakage fluid dram, the leakage fluid dram, is fixed with discharging tube, and the discharging tube connects
Testing agency is met, the testing agency is connected by pipeline and plasma constitution is provided with waste liquid recovery apparatus, the testing agency
Spectrometer.
It is preferred that, the amberplex includes ion exchange membrane sheet and enhancing gauze, and the enhancing gauze is electrically conductive
Gauze, it is woven or is entwined by some electrically conductive yarns, provided with enhancing gauze, the increasing between the ion exchange membrane sheet
It is provided with sprayed coating, the sprayed coating and is coated with the outside of strong gauze and ion exchange membrane sheet linear contact lay, the ion exchange membrane sheet
Antistatic additive.
It is preferred that, the testing agency bottom is provided with the first pipeline and second pipe, and first pipeline and the second pipe
The first magnetic valve and the second magnetic valve are respectively equipped with road, first pipeline connects waste liquid recovery apparatus, the second pipe
Connect feed tube.
Compared with prior art, the beneficial effects of the utility model are：
(1) the utility model structural principle is simple, easy to operate, and the heavy metal ion in sewage quickly can be divided
From using testing agency, being detected to the sewage after separation, qualified liquid is directly discharged into retracting device, unqualified
Sewage be discharged into again in electrolytic cell and carry out multi-cycle separation, improve disintegrate-quality.
(2) the ion exchange film-strength that the utility model is used is big, antistatic effect is good, it is to avoid electrostatic causes ion to be handed over
Change film working effect not good enough, further increase separating effect.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Fig. 2 is amberplex sectional view of the present utility model.
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 obtained, belongs to the scope of the utility model protection.
Fig. 1-2 is referred to, the utility model provides a kind of technical scheme：A kind of katholysis Heavy metal separation device,
Including electrolytic cell 1, the upper end of electrolytic cell 1 is provided with upper end cover 2, and the inner chamber of electrolytic cell 1 is provided with amberplex 3, it is described from
The both sides of proton exchange 3 are respectively equipped with minus plate 4 and positive plate 5, and the upper end cover 2 connects provided with negative terminal 6 and positive pole
Line terminals 7 and inlet opening 8, the connection of negative terminal 6 minus plate 4, the jointed anode plate 5 of positive terminal 7,
Feed tube 9 is fixed with the inlet opening 8, the bottom of electrolytic cell 1 is provided with fixation in leakage fluid dram 10, the leakage fluid dram 10 and set
There is discharging tube 11, the connecting detection mechanism of discharging tube 11, the testing agency connects waste liquid recovery apparatus 12, institute by pipeline
State and plasma mass spectrograph 13 is provided with testing agency.
In the present embodiment, amberplex 3 includes ion exchange membrane sheet 14 and enhancing gauze 15, and the enhancing gauze 15 is
Electrically conductive gauze, it is woven or is entwined by some electrically conductive yarns, provided with enhancing yarn between the ion exchange membrane sheet 14
Net 15, the enhancing gauze 15 and the linear contact lay of ion exchange membrane sheet 14, the outside of ion exchange membrane sheet 14 are provided with sprayed coating 16,
Antistatic additive is coated with the sprayed coating 16, the ion exchange film-strength that the utility model is used is big, and antistatic effect is good, keeps away
Having exempted from electrostatic causes amberplex working effect not good enough, further increases separating effect.
In addition, in the present embodiment, testing agency bottom is provided with the first pipeline 17 and second pipe 18, and first pipeline
17 and second pipe 18 on be respectively equipped with the first magnetic valve 19 and the second magnetic valve 20, first pipeline 17 connects devil liquor recovery
Device 12, the second pipe 18 connects feed tube 9.
The utility model structural principle is simple, easy to operate, can carry out quick separating to the heavy metal ion in sewage,
Using testing agency, the sewage after separation can be detected, qualified liquid is directly discharged into retracting device, underproof dirt
Water is discharged into electrolytic cell again carries out multi-cycle separation, improves disintegrate-quality.
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 in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (3)
1. a kind of katholysis Heavy metal separation device, including electrolytic cell (1), it is characterised in that：Electrolytic cell (1) upper end
Provided with upper end cover (2), electrolytic cell (1) inner chamber is provided with amberplex (3), and amberplex (3) both sides are set respectively
Have a minus plate (4) and positive plate (5), the upper end cover (2) provided with negative terminal (6) and positive terminal (7) with
And inlet opening (8), negative terminal (6) the connection minus plate (4), positive terminal (7) the jointed anode plate
(5) feed tube (9), is fixed with the inlet opening (8), electrolytic cell (1) bottom is provided with leakage fluid dram (10), the discharge opeing
Discharging tube (11) is fixed with mouth (10), discharging tube (11) the connecting detection mechanism, the testing agency is connected by pipeline
Connect and plasma mass spectrograph (13) is provided with waste liquid recovery apparatus (12), the testing agency.
2. a kind of katholysis Heavy metal separation device according to claim 1, it is characterised in that：The ion exchange
Film (3) includes ion exchange membrane sheet (14) and enhancing gauze (15), and the enhancing gauze (15) is electrically conductive gauze, and it is by some
Electrically conductive yarn braiding is entwined, provided with enhancing gauze (15), the enhancing yarn between the ion exchange membrane sheet (14)
Sprayed coating (16), the spray are provided with the outside of net (15) and ion exchange membrane sheet (14) linear contact lay, the ion exchange membrane sheet (14)
Coating is coated with antistatic additive on (16).
3. a kind of katholysis Heavy metal separation device according to claim 1, it is characterised in that：The testing agency
Bottom is provided with the first pipeline (17) and second pipe (18), and first pipeline (17) and second pipe (18) and is respectively equipped with
First magnetic valve (19) and the second magnetic valve (20), the first pipeline (17) connection waste liquid recovery apparatus (12), described second
Pipeline (18) connection feed tube (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621478189.6U CN206511967U (en) | 2016-12-30 | 2016-12-30 | A kind of katholysis Heavy metal separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621478189.6U CN206511967U (en) | 2016-12-30 | 2016-12-30 | A kind of katholysis Heavy metal separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206511967U true CN206511967U (en) | 2017-09-22 |
Family
ID=59864014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621478189.6U Expired - Fee Related CN206511967U (en) | 2016-12-30 | 2016-12-30 | A kind of katholysis Heavy metal separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206511967U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110079828A (en) * | 2019-05-21 | 2019-08-02 | 西安汇创贵金属新材料研究院有限公司 | A kind of processing unit and processing method of gold electrolyte |
| CN110723771A (en) * | 2019-11-07 | 2020-01-24 | 伊犁新天煤化工有限责任公司 | Novel phenol ammonia recovery device for efficiently recovering ammonia |
-
2016
- 2016-12-30 CN CN201621478189.6U patent/CN206511967U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110079828A (en) * | 2019-05-21 | 2019-08-02 | 西安汇创贵金属新材料研究院有限公司 | A kind of processing unit and processing method of gold electrolyte |
| CN110079828B (en) * | 2019-05-21 | 2021-04-13 | 西安汇创贵金属新材料研究院有限公司 | Treatment device and treatment method for gold electrolysis waste liquid |
| CN110723771A (en) * | 2019-11-07 | 2020-01-24 | 伊犁新天煤化工有限责任公司 | Novel phenol ammonia recovery device for efficiently recovering ammonia |
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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 |
Granted publication date: 20170922 Termination date: 20201230 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |