CN207391132U - Electroplating effluent heavy metal piece-rate system - Google Patents
Electroplating effluent heavy metal piece-rate system Download PDFInfo
- Publication number
- CN207391132U CN207391132U CN201720278008.3U CN201720278008U CN207391132U CN 207391132 U CN207391132 U CN 207391132U CN 201720278008 U CN201720278008 U CN 201720278008U CN 207391132 U CN207391132 U CN 207391132U
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- CN
- China
- Prior art keywords
- reaction tank
- heavy metal
- sedimentation basin
- head cover
- coagulation reaction
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Abstract
The utility model discloses electroplating effluent heavy metal piece-rate system, including condenser, head cover, pH value detector, coagulation reaction tank, filter screen, leakage fluid dram, support base, fixing bracket, slag-drip opening, sedimentation basin, hydrogen sulfide gas access tube, fixed card buckle, air inlet, gas backstreaming pipe and condenser pipe.The condenser pipe is internally provided with condenser, one end of the gas backstreaming pipe is connected with condenser pipe, head cover is provided with below the condenser pipe, the outside of the head cover is provided with fixed card buckle, and the coagulation reaction tank is internally provided with hydrogen sulfide gas access tube.Heavy metal ion is deposited in the form of sulfide inside sedimentation basin, it will be after internal waste liquid discharge by leakage fluid dram, precipitation is discharged by slag-drip opening, the separation of heavy metal can be realized, there is provided the gas backstreaming pipes of hydrogen sulfide gas, the hydrogen sulfide gas for having little time reaction can be passed by hydrogen sulfide gas access tube inside coagulation reaction tank again, save material.
Description
Technical field
The utility model is related to electroplating wastewater treatment device, more particularly to electroplating effluent heavy metal piece-rate system, belong to point
From engineering device technique field.
Background technology
It is well known that cupper smelting has the electricity of cupric, nickel, acid and various metals impurity daily in copper electrolytic process
Liquid waste solution needs periodically open circuit discharge；Rare precious metal extraction enterprise, paper tinsel electrolysis electroplating enterprise, circuit board etching enterprise equally need
It periodically to discharge containing acid（Containing alkali）, waste liquid containing heavy metal, therefore, after the open circuit discharge of these waste liquids, if purified treatment and
Which type of handled with technology mode, whether valuable metal and soda acid recycle, and just become current China's environmental pollution and environmental protection, close
People's health, the major issue of quality of life living environment, arrived the whole people pay attention to and make laws emphasis regulation project it
One, in addition, how to administer, using what technology mode, it is related to existence and the economic benefit of ten million enterprise.It there is now and extensive
The contaminated liquid purification style used mainly has Physical chemical method bioanalysis three categories, it should say that method is various, such as without considering into
This factor has plenty of individual event, has plenty of two or the combination of multinomial process configures and all obtained purification and impurity removal recycling
The remarkable result utilized.
There are the knots of some defects, such as piece-rate system in use for existing electroplating effluent heavy metal piece-rate system
Structure is complicated, equipment investment is high and piece-rate system on be not provided with pH value detector, it is impossible to detect that internal heavy metal sinks
The effect in shallow lake is not provided with gas reflux apparatus, and separated efficiency is than relatively low.
Utility model content
The utility model provides electroplating effluent heavy metal piece-rate system, can efficiently solve and be carried in doctor's background above technology
The piece-rate system gone out it is complicated, equipment investment is high and piece-rate system on be not provided with pH value detector, it is impossible to detect
To the effect of internal heavy metal precipitation, be not provided with gas reflux apparatus, separated efficiency than it is relatively low the problem of.
In order to solve the above-mentioned technical problem, the utility model provide electroplating effluent heavy metal piece-rate system, including condenser,
Head cover, pH value detector, coagulation reaction tank, filter screen, leakage fluid dram, support base, fixing bracket, slag-drip opening, sedimentation basin, vulcanization
Hydrogen access tube, fixed card buckle, air inlet, gas backstreaming pipe and condenser pipe, the condenser pipe are internally provided with condenser,
One end of the gas backstreaming pipe is connected with condenser pipe, and the other end of gas backstreaming pipe is connected with air inlet, the condenser pipe
Lower section be provided with head cover, the outside of the head cover is provided with fixed card buckle, and coagulation reaction tank is provided with below head cover, institute
That states coagulation reaction tank is internally provided with hydrogen sulfide gas access tube, and pH value detection is provided with above the right side of coagulation reaction tank
Instrument is provided with sedimentation basin below the coagulation reaction tank, filter screen is provided on the right side of the sedimentation basin, the filter screen
Right side is provided with leakage fluid dram, and the lower section middle position of the sedimentation basin is provided with slag-drip opening, the lower right-hand side of the sedimentation basin
Fixing bracket is provided with, and support bracket fastened lower section is provided with support base, the pH value detector and external control panel electricity
Property connection.
Preferably, the head cover is fixedly connected with coagulation reaction tank by fixed card buckle.
Preferably, there are two the fixing bracket is set altogether, and two fixing brackets are separately positioned below sedimentation basin and lean on
The left and right sides of nearly slag-drip opening.
Preferably, the support base is fixedly connected with sedimentation basin by fixing bracket.
Preferably, the head cover is an integral structure with condenser pipe.
The advantageous effect that the utility model is reached is：The structure of this piece-rate system is simple, by coagulation reaction tank and precipitation
Pond is combined together, and is provided with filter screen in the one side of sedimentation basin leakage fluid dram, it would be desirable to which separated electroplating effluent is passed into one's duty
From internal system, hydrogen sulfide gas is passed through from air inlet, it is anti-that hydrogen sulfide gas is passed into coagulation from hydrogen sulfide gas access tube
The bottom of Ying Chi, by chemical reaction, heavy metal ion is deposited in the form of sulfide inside sedimentation basin, will by leakage fluid dram
After internal waste liquid discharge, precipitate and discharged by slag-drip opening, you can realize the separation of heavy metal, there is provided the gases of hydrogen sulfide gas
The hydrogen sulfide gas for having little time reaction can be passed by hydrogen sulfide gas access tube in coagulation reaction tank by return duct again
Portion saves material, and there is provided pH value testers, can detect internal precipitation process in real time.
Description of the drawings
Attached drawing is used to provide a further understanding of the present invention, and a part for constitution instruction, with this practicality
New embodiment for explaining the utility model, does not form the limitation to the utility model together.In the accompanying drawings：
Fig. 1 is the structure diagram of the utility model；
Fig. 2 is the top view of the utility model；
In figure：1st, condenser；2nd, head cover；3rd, pH value detector；4th, coagulation reaction tank；5th, filter screen；6th, leakage fluid dram；7th, prop up
Support pedestal；8th, fixing bracket；9th, slag-drip opening；10th, sedimentation basin；11st, hydrogen sulfide gas access tube；12nd, fixed card buckle；13rd, air inlet
Mouthful；14th, gas backstreaming pipe；15th, condenser pipe.
Specific embodiment
The preferred embodiment of the utility model is illustrated below in conjunction with attached drawing, it should be understood that described herein excellent
Embodiment is selected to be only used for describing and explaining the present invention, is not used to limit the utility model.
- 2 are please referred to Fig.1, the utility model provides a kind of technical solution：Including condenser 1, head cover 2, pH value detector 3,
Coagulation reaction tank 4, filter screen 5, leakage fluid dram 6, support base 7, fixing bracket 8, slag-drip opening 9, sedimentation basin 10, hydrogen sulfide gas connect
Enter pipe 11, fixed card buckle 12, air inlet 13, gas backstreaming pipe 14 and condenser pipe 15, condenser pipe 15 is internally provided with condenser
1, one end of gas backstreaming pipe 14 is connected with condenser pipe 15, and the other end of gas backstreaming pipe 14 is connected with air inlet 13, condensation
The lower section of pipe 15 is provided with head cover 2, and the outside of head cover 2 is provided with fixed card buckle 12, and the lower section of head cover 2 is provided with coagulating
Pond 4, coagulation reaction tank 4 is internally provided with hydrogen sulfide gas access tube 11, and is provided with pH above the right side of coagulation reaction tank 4
It is worth detector 3, the lower section of coagulation reaction tank 4 is provided with sedimentation basin 10, and the right side of sedimentation basin 10 is provided with filter screen 5, filter screen 5
Right side be provided with leakage fluid dram 6, the lower section middle position of sedimentation basin 10 is provided with slag-drip opening 9, the lower right-hand side of sedimentation basin 10
Fixing bracket 8 is provided with, and the lower section of fixing bracket 8 is provided with support base 7, pH value detector 3 and external control panel electricity
Property connection.
In order to make to stablize between head cover 2 and coagulation reaction tank 4 fixation, in the present embodiment, it is preferred that head cover 2 with it is mixed
Solidifying reaction tank 4 is fixedly connected by fixed card buckle 12.
In order to which the structure of this piece-rate system is made more to stablize, in the present embodiment, it is preferred that fixing bracket 8 is provided with two altogether
It is a, and two fixing brackets 8 are separately positioned on 10 lower section of sedimentation basin close to the left and right sides of slag-drip opening 9.
In order to which the structure of this piece-rate system is made more to stablize, in the present embodiment, it is preferred that support base 7 and sedimentation basin 10
It is fixedly connected by fixing bracket 8.
In order to which the structure of this piece-rate system is made more to stablize, in the present embodiment, it is preferred that head cover 2 is one with condenser pipe 15
Body formula structure.
The operation principle and process for using of the utility model：Coagulation reaction tank 4 and sedimentation basin 10 are combined together, heavy
The one side of 10 leakage fluid dram 6 of shallow lake pond is provided with filter screen 5, it would be desirable to and separated electroplating effluent is passed into this separation internal system, from
Air inlet 13 is passed through hydrogen sulfide gas, and hydrogen sulfide gas is passed into the bottom of coagulation reaction tank 4 from hydrogen sulfide gas access tube 11
Portion, by chemical reaction, heavy metal ion is deposited in the form of sulfide inside sedimentation basin 10, by leakage fluid dram 6 by inside
Waste liquid discharge after, precipitate and discharged by slag-drip opening 9, you can realize the separation of heavy metal, there is provided hydrogen sulfide gas gas return
The hydrogen sulfide gas for having little time reaction can be passed into coagulation reaction tank 4 by flow tube 14 by hydrogen sulfide gas access tube 11 again
Inside saves material, and there is provided pH value testers 3, can detect internal precipitation process in real time.
Finally it should be noted that：The above is only the preferred embodiment of the utility model only, is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical solution recorded in foregoing embodiments or to which part technical characteristic
Carry out equivalent substitution.Within the spirit and principle of the utility model, any modifications, equivalent replacements and improvements are made,
It should be included within the scope of protection of this utility model.
Claims (5)
1. electroplating effluent heavy metal piece-rate system, including condenser（1）, head cover（2）, pH value detector（3）, coagulation reaction tank
（4）, filter screen（5）, leakage fluid dram（6）, support base（7）, fixing bracket（8）, slag-drip opening（9）, sedimentation basin（10）, stink damp
Body access tube（11）, fixed card buckle（12）, air inlet（13）, gas backstreaming pipe（14）And condenser pipe（15）, the condenser pipe
（15）Be internally provided with condenser（1）, the gas backstreaming pipe（14）One end be connected with condenser pipe（15）, and gas backstreaming
Pipe（14）The other end and air inlet（13）Connection, the condenser pipe（15）Lower section be provided with head cover（2）, the head cover（2）
Outside be provided with fixed card buckle（12）, and head cover（2）Lower section be provided with coagulation reaction tank（4）, the coagulation reaction tank（4）
Be internally provided with hydrogen sulfide gas access tube（11）, and coagulation reaction tank（4）Right side above be provided with pH value detector
（3）, the coagulation reaction tank（4）Lower section be provided with sedimentation basin（10）, the sedimentation basin（10）Right side be provided with filter screen
（5）, the filter screen（5）Right side be provided with leakage fluid dram（6）, the sedimentation basin（10）Lower section middle position be provided with row
Cinder notch（9）, the sedimentation basin（10）Lower right-hand side be provided with fixing bracket（8）, and fixing bracket（8）Lower section be provided with branch
Support pedestal（7）, the pH value detector（3）It is electrically connected with external control panel.
2. electroplating effluent heavy metal piece-rate system according to claim 1, it is characterised in that：The head cover（2）With coagulation
Reaction tank（4）Pass through fixed card buckle（12）It is fixedly connected.
3. electroplating effluent heavy metal piece-rate system according to claim 1, it is characterised in that：The fixing bracket（8）Altogether
There are two settings, and two fixing brackets（8）It is separately positioned on sedimentation basin（10）Lower section is close to slag-drip opening（9）The left and right sides.
4. electroplating effluent heavy metal piece-rate system according to claim 1, it is characterised in that：The support base（7）With
Sedimentation basin（10）Pass through fixing bracket（8）It is fixedly connected.
5. electroplating effluent heavy metal piece-rate system according to claim 1, it is characterised in that：The head cover（2）With condensation
Pipe（15）It is an integral structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720278008.3U CN207391132U (en) | 2017-03-21 | 2017-03-21 | Electroplating effluent heavy metal piece-rate system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720278008.3U CN207391132U (en) | 2017-03-21 | 2017-03-21 | Electroplating effluent heavy metal piece-rate system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207391132U true CN207391132U (en) | 2018-05-22 |
Family
ID=62401749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720278008.3U Expired - Fee Related CN207391132U (en) | 2017-03-21 | 2017-03-21 | Electroplating effluent heavy metal piece-rate system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207391132U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092006A (en) * | 2018-10-15 | 2018-12-28 | 南安市博胤机械科技有限公司 | A kind of mercury vapour protection inspection cover of electrolytic salt Industrial Wastewater Treatment tank |
| CN111411229A (en) * | 2020-04-29 | 2020-07-14 | 长沙华时捷环保科技发展股份有限公司 | Process for efficiently separating nickel and copper in nickel electrolyte |
-
2017
- 2017-03-21 CN CN201720278008.3U patent/CN207391132U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092006A (en) * | 2018-10-15 | 2018-12-28 | 南安市博胤机械科技有限公司 | A kind of mercury vapour protection inspection cover of electrolytic salt Industrial Wastewater Treatment tank |
| CN111411229A (en) * | 2020-04-29 | 2020-07-14 | 长沙华时捷环保科技发展股份有限公司 | Process for efficiently separating nickel and copper in nickel electrolyte |
| CN111411229B (en) * | 2020-04-29 | 2021-04-09 | 长沙华时捷环保科技发展股份有限公司 | Process for efficiently separating nickel and copper in nickel electrolyte |
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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: 20180522 Termination date: 20200321 |