CN203007447U - Electrolytic bath suitable for titanium cathode plate - Google Patents
Electrolytic bath suitable for titanium cathode plate Download PDFInfo
- Publication number
- CN203007447U CN203007447U CN2012206899703U CN201220689970U CN203007447U CN 203007447 U CN203007447 U CN 203007447U CN 2012206899703 U CN2012206899703 U CN 2012206899703U CN 201220689970 U CN201220689970 U CN 201220689970U CN 203007447 U CN203007447 U CN 203007447U
- Authority
- CN
- China
- Prior art keywords
- collecting bin
- cell body
- metal
- negative plate
- collecting
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
The utility model relates to an electrolytic bath suitable for a titanium cathode plate. The electrolytic bath comprises a bath body, wherein an ionic exchange membrane is arranged in the bath body; the bath body is divided into an anode chamber and a cathode chamber by the ionic exchange membrane; a discharge hopper is arranged at the bottom of the bath body, and connected with the cathode chamber; a titanium cathode plate is arranged between the anode chamber and the cathode chamber; the discharge hopper is connected with a liquid outlet tube to drain an electrolytic waste liquid; and a collection bin for collecting precipitated metal is arranged at the bottom of the discharge hopper; and the inlet of the collection bin is connected with the bottom of the discharge hopper. The electrolytic bath is used for collecting precipitated metal through the collection bin, and collecting all the precipitates, so that electrolysis and collection can be separated and independent, and the electrolysis efficiency can be improved.
Description
Technical field
The utility model relates to a kind of electrolyzer that is applicable to titanium negative plate.
Background technology
The circuit-board industry development of current China is swift and violent, often contain a large amount of metallicses with recovery value in the waste water of producing due to board production enterprise, and heavy metals exceeding standard is serious, particularly also has a large amount of cupric ions in etching solution, its discharging meeting brings great harm to environment, so how to extract the cupric ion in etching solution, the production efficiency that improves electrolytic copper is the technical barrier of this area, and traditional electrolyzer is very single, can't the electrolysis various metals.
The utility model content
The technical problems to be solved in the utility model is to provide a kind of electrolytic efficiency that is suitable for improving, the convenient electrolyzer that is applicable to titanium negative plate that takes out precipitating metal.
In order to address the above problem, the utility model provides a kind of electrolyzer that is applicable to titanium negative plate, comprise: cell body, be provided with ion-exchange membrane in described cell body, described ion-exchange membrane is divided into anolyte compartment and cathode compartment with described cell body, is provided with titanium negative plate between described anolyte compartment and cathode compartment; The bottom of described cell body is also established one and is gone out funnel, and describedly goes out funnel and be connected with described cathode compartment;
Describedly go out funnel and be connected with a drain pipe with the discharging electrolysis waste solution;
Establish a collecting bin that is suitable for collecting the metal of separating out in the described bottom that goes out funnel, and the entrance of this collecting bin is connected with the described bottom that goes out funnel.
Further, central processing unit, the bottom of described collecting bin is provided with discharge opening, a weight sensor is established to detect the weight of the metal in collecting bin in bottom in collecting bin, this weight sensor is connected with described central processing unit, establish a valve in the ingress of described collecting bin, this valve and discharge opening are controlled by central processing unit;
Wherein, described central processing unit cuts out described valve when described weight sensor detects metal that described collecting bin collects and reaches certainweight, and opens discharge opening and unload metal in collecting bin.
Compared with prior art, the electrolyzer that is applicable to titanium negative plate of the present utility model has following advantage: independently control the compensation problem that has realized the uneven output of three-phase supply by minute phase current; By collecting bin, precipitating metal is collected, what can be realized separating out what are collected, accomplish electrolysis and collect two work separately, independent mutually; When the metal in collecting bin reached certainweight, shut-off valve prevented that liquid from flowing out, and the assurance etching solution is proceeded reaction in electrolyzer, but carry out simultaneously discharging work, when discharging finishes, close discharge opening, control valve is opened and is continued to collect the metal of separating out, and has greatly improved production efficiency; After the metal of etching solution was complete by electrolysis, waste liquid was discharged from drain pipe, can not wash out the metal of collecting bin in discharge process; Can also electrolysis go out nickel by titanium negative plate, increase the efficient of electrolysis.By collecting bin, precipitating metal is collected, what can be realized separating out what are collected, accomplish electrolysis and collect two work separately, independent mutually; When the metal in collecting bin reached certainweight, shut-off valve prevented that liquid from flowing out, and the assurance etching solution is proceeded reaction in electrolyzer, but carry out simultaneously discharging work, when discharging finishes, close discharge opening, control valve is opened and is continued to collect the metal of separating out, and has greatly improved production efficiency; After the metal of etching solution was complete by electrolysis, waste liquid was discharged from drain pipe, can not wash out the metal of collecting bin in discharge process.
Description of drawings
For content of the present utility model is more likely to be clearly understood, below the specific embodiment and by reference to the accompanying drawings of basis, the utility model is described in further detail, wherein
Fig. 1 structural representation that is applicable to the electrolyzer of titanium negative plate of the present utility model.
Embodiment
Below in conjunction with drawings and Examples, the utility model is elaborated:
As shown in Figure 1, a kind of electrolyzer that is applicable to titanium negative plate comprises: cell body 1, be provided with ion-exchange membrane in described cell body, and described ion-exchange membrane is divided into anolyte compartment and cathode compartment with described cell body, is provided with titanium negative plate between described anolyte compartment and cathode compartment; The bottom of described cell body is also established one and is gone out funnel 2, and describedly goes out funnel 2 and be connected with described cathode compartment;
Describedly go out funnel 2 and be connected with a drain pipe 3 with the discharging electrolysis waste solution;
Establish a collecting bin 4 that is suitable for collecting the metal of separating out in the described bottom that goes out funnel 2, and the entrance of this collecting bin 4 is connected with the described bottom that goes out funnel 2.
The described electrolyzer that is applicable to titanium negative plate also comprises: central processing unit, the bottom of described collecting bin 4 is provided with discharge opening 4-1, a weight sensor is established to detect the weight of the metal in collecting bin 4 in bottom in collecting bin 4, this weight sensor is connected with described central processing unit, establish a valve 4-2 in the ingress of described collecting bin 4, this valve 4-2 and discharge opening are controlled by central processing unit;
Wherein, described central processing unit cuts out described valve 4-2 when described weight sensor detects metal that described collecting bin 4 collects and reaches certainweight, and opens discharge opening 4-1 and unload metal in collecting bin 4.
Establish one at described drain pipe 3 and control the bleed valve 3-1 that electrolysis waste solution discharges, namely in the time of electrolytic reaction, close this bleed valve 3-1.
Obviously, above-described embodiment is only for the utility model example clearly is described, and is not to be restriction to embodiment of the present utility model.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here need not also can't give all embodiments exhaustive.And these belong to apparent variation or the change that spirit of the present utility model extended out and still are among protection domain of the present utility model.
Claims (1)
1. electrolyzer that is applicable to titanium negative plate, it is characterized in that comprising: titanium negative plate, cell body, be provided with ion-exchange membrane in described cell body, described ion-exchange membrane is divided into anolyte compartment and cathode compartment with described cell body, it is characterized in that, be provided with titanium negative plate between described anolyte compartment and cathode compartment; The bottom of described cell body is also established one and is gone out funnel, and describedly goes out funnel and be connected with described cathode compartment;
Describedly go out funnel and be connected with a drain pipe with the discharging electrolysis waste solution;
Establish a collecting bin that is suitable for collecting the metal of separating out in the described bottom that goes out funnel, and the entrance of this collecting bin is connected with the described bottom that goes out funnel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206899703U CN203007447U (en) | 2012-12-13 | 2012-12-13 | Electrolytic bath suitable for titanium cathode plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206899703U CN203007447U (en) | 2012-12-13 | 2012-12-13 | Electrolytic bath suitable for titanium cathode plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203007447U true CN203007447U (en) | 2013-06-19 |
Family
ID=48599059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012206899703U Expired - Fee Related CN203007447U (en) | 2012-12-13 | 2012-12-13 | Electrolytic bath suitable for titanium cathode plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203007447U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103103575A (en) * | 2012-12-13 | 2013-05-15 | 苏州新区化工节能设备厂 | Electrolyser applicable to titanium cathode plates |
-
2012
- 2012-12-13 CN CN2012206899703U patent/CN203007447U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103103575A (en) * | 2012-12-13 | 2013-05-15 | 苏州新区化工节能设备厂 | Electrolyser applicable to titanium cathode plates |
| CN103103575B (en) * | 2012-12-13 | 2015-10-28 | 苏州赛斯德工程设备有限公司 | A kind of electrolyzer being applicable to titanium negative plate |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104131285B (en) | The recovery method of ferric trichloride etching waste liquor | |
| CN103397348B (en) | A kind of method utilizing the cyclone electrolytic cell process anode sludge | |
| CN107012466B (en) | A kind of acidic etching liquid method for recycling and system | |
| CN102303917A (en) | Method for mixed treatment of waste liquid from acid etching and micro etching of printed circuit boards | |
| CN109264831A (en) | Asymmetric capacitor desalter and the method that desalination is carried out using the device | |
| CN203007441U (en) | Water electrolytic bath | |
| CN209132046U (en) | A kind of water sampling unit for environmentally friendly water quality detection | |
| CN203007447U (en) | Electrolytic bath suitable for titanium cathode plate | |
| CN102010036A (en) | Treatment method of waste silver electrolyte | |
| CN203007442U (en) | Ionic membrane electrolytic bath | |
| CN210885679U (en) | Pretreatment device is collected to electrolytic copper's waste liquid | |
| CN104726866A (en) | Acidic etching waste liquid regeneration and copper recovery device | |
| CN204138483U (en) | Pickling nickel waste water reclaims cyclic regeneration device | |
| CN203382824U (en) | Device for recovering refined copper from low-copper-content wastewater | |
| CN206580676U (en) | A kind of metal recovery and tapping equipment | |
| CN203320173U (en) | Electroplating wastewater recycling discharge reduction device | |
| CN206511967U (en) | A kind of katholysis Heavy metal separation device | |
| CN109208032A (en) | A method of gallium is recycled from electrodeposition in alkaline solution containing gallium | |
| CN201678496U (en) | Electroplating waste water electrolytic tank with hydraulic cyclone separator | |
| CN104817137B (en) | A kind of standard zero polar distance electrolytic bath processed for water | |
| CN104357881A (en) | Electrolysis system based on fully sealed selective powder electrolysis device | |
| CN204417260U (en) | A kind for the treatment of system of lower concentration copper-containing wastewater | |
| CN204251731U (en) | A kind of hermetically sealed selectivity small test electrolyzer | |
| CN108288736B (en) | Sulfuric acid dechlorination system for waste lead-acid storage battery and dechlorination method using same | |
| CN210085182U (en) | Coal gasification grey water treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130619 Termination date: 20131213 |