CN213142227U - Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution - Google Patents

Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution Download PDF

Info

Publication number
CN213142227U
CN213142227U CN202021684480.5U CN202021684480U CN213142227U CN 213142227 U CN213142227 U CN 213142227U CN 202021684480 U CN202021684480 U CN 202021684480U CN 213142227 U CN213142227 U CN 213142227U
Authority
CN
China
Prior art keywords
positive pole
etching
anode
support frame
copper
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.)
Active
Application number
CN202021684480.5U
Other languages
Chinese (zh)
Inventor
罗国华
顾晓聪
刘碧华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Zhending Environmental Technology Co ltd
Original Assignee
Guangdong Zhending Environmental Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangdong Zhending Environmental Technology Co ltd filed Critical Guangdong Zhending Environmental Technology Co ltd
Priority to CN202021684480.5U priority Critical patent/CN213142227U/en
Application granted granted Critical
Publication of CN213142227U publication Critical patent/CN213142227U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

The utility model relates to an electrolysis equipment technical field, concretely relates to ion exchange membrane electrolysis trough and acid etching solution regeneration recycle copper recovery plant, this ion exchange membrane electrolysis trough include the cell body, are equipped with two at least negative plates and at least one positive pole box in the cell body, and the negative plate sets up with positive pole box interval, and positive pole box includes support frame, anode plate and two positive pole ionic membrane, and the anode plate is pegged graft in the support frame, and two positive pole ionic membrane are located the both sides of anode plate, the support frame is made by the titanium net, and the titanium net of support frame both sides passes through the resistance detection device electricity with adjacent negative plate and is connected, and the resistance detection device electricity is connected with audible-visual annunciator. The utility model discloses an ionic membrane electrolytic cell is through adopting resistance detection device to measure the resistance between titanium net and the adjacent negative plate, is less than the setting value when resistance, produces alarm signal, is zero when resistance, can send audible-visual annunciation at this moment, and the operator in time handles, can prevent like this that the ionic membrane from impaling.

Description

Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution
Technical Field
The utility model relates to an electrolysis equipment technical field, concretely relates to ion membrane electrolysis trough and acid etching solution regeneration recycle copper recovery plant.
Background
The ion exchange membrane electrolysis method is a new technology developed on the basis of ion exchange resin, and utilizes the characteristic that the ion exchange membrane has selective permeability to anions and cations to allow ions with one charge to pass through and limit ions with opposite charges to pass through so as to achieve the purposes of concentration, desalination, purification and electrochemical synthesis.
At present, in the etching process of the ionic membrane on the circuit board, the concentration of copper ions in the etching solution can be gradually increased to reduce the etching effect, and the copper ions (Cu) in the etching solution must be used for achieving the best etching effect of the etching solution+) Redox number, chloride ion (Cl)-) And the acid equivalent is kept in a reasonable and stable range, and the continuous addition of the sub-solution is required to replace the waste etching solution which loses the etching capability in order to keep the optimum concentration of the above-mentioned components in the etching solution. In the manufacturing process of the printed circuit board, the recycling and regeneration of the acidic copper chloride etching solution always troubles the enterprises of the printed circuit board, the non-renewable acidic copper chloride etching solution contains about 100 to 130 grams of copper per liter, and the copper content of the waste etching solution generated in every month in Guangdong province is as high as thousands of tons, so that the recycling of the metal copper and the recycling and regeneration of the waste etching solution inevitably have great economic benefit and environmental protection value.
At present, many units for researching and developing copper chloride etching solution electrolysis recovery copper at home and abroad are available, including many scientific research institutions, universities and the like, other problems occur in the use process of the researched and developed equipment, so that the researched and developed equipment cannot be put into industry, if the etching solution cannot be recycled after copper is extracted through electrolysis, the transfer of pollution sources also causes secondary pollution to the environment, meanwhile, chlorine is separated out from an anode in the electrolysis process, according to the theoretical calculation, 111.6kg of chlorine is separated out from the anode every time 100kg of copper is separated out through electrolysis, and the volume of the copper chloride in the standard state is about 35.26m3However, the cost and equipment complexity are increased by properly treating the large amount of chlorine gas generated and the residual waste liquid without causing secondary pollution to the environment.
The on-line regeneration process of the chemical liquid is an on-line regeneration process, namely, electrolytic regeneration equipment is connected with an etching machine in series, and the pair of reactions of regeneration reaction and etching reaction which are mutually reversible are carried out in a circulating mode in turn. The electro-catalytic coating electrode is used as an anode, and the potential difference between the anode and anolyte is used as a reaction driving force, so that cuprous complex ions on the surface of the anode are oxidized into copper complex ions, and the oxidation regeneration of the etching waste liquid is realized; and (3) establishing a copper concentration difference between the anolyte and the catholyte, and under the promotion of electrochemical potential and chemical potential, part of copper ions are transferred to a cathode region, so that the specific gravity of the acidic etching solution is reduced to a certain range, or the specific gravity of the etching solution is adjusted by using the catholyte in an auxiliary way, so that the chemical composition, the oxidation-reduction potential and the specific gravity of the acidic etching waste solution are recovered as before.
By the perfect combination of the device and the process, the economic problem and the environmental protection problem which puzzle the PCB industry for years of waste etching liquid reutilization are finally solved.
The 'ionic membrane copper electrolysis' process is adopted, and the process is that an anode area and a cathode area of an electrolytic bath are divided into two independent areas by the ionic membrane; the anode area is a waste etching solution regeneration area, and univalent copper ions in the waste etching solution after copper reduction are subjected to electrochemical reaction to generate bivalent copper ions so as to regenerate the waste etching solution; the cathode area is a copper recovery area, ions in the solution are selectively and directionally transferred through an ion diaphragm, and copper ions in the solution are reduced into zero-valent copper through electrons.
However, the conventional apparatus has a problem that the ionic membrane is easily damaged. In the process of copper electroplating, copper plating layers are easy to grow long copper nails, and sharp copper nails are easy to pierce the ion exchange membrane. Ion exchange membranes are unusually expensive and damage to the ion membrane causes significant losses. Meanwhile, the damaged ionic membrane causes mixing of the anolyte and the catholyte, corrosion of the copper plating layer, increase of energy consumption of copper plating and increase of cost.
Disclosure of Invention
In order to overcome the shortcoming and the deficiency that exist among the prior art, the utility model aims to provide an ion membrane electrolysis trough, this ion membrane electrolysis trough can early warning copper nail produce with the harm of prevention copper nail, simple structure, convenient to use, it is with low costs.
Another object of the present invention is to provide a copper recycling apparatus for recycling acidic etching solution.
The purpose of the utility model is realized through the following technical scheme: the utility model provides an ion membrane electrolytic cell, includes the cell body, is equipped with two at least negative plates and at least one positive pole box in the cell body, and negative plate and positive pole box interval set up, and positive pole box includes support frame, anode plate and two positive pole ionic membrane, and the anode plate is pegged graft in the support frame, and two positive pole ionic membrane are located the both sides of anode plate, the support frame is made by the titanium net, and the titanium net of support frame both sides is connected through resistance detection device electricity with adjacent negative plate, and resistance detection device electricity is connected with audible-visual annunciator.
The other purpose of the utility model is realized by the following technical scheme: the ionic membrane copper recovery equipment is the ionic membrane electrolytic cell.
Furthermore, the ionic membrane copper recovery equipment further comprises a circulating tank, an etching production line, an etching waste liquid collecting tank and an etching waste liquid storage tank, wherein the ionic membrane electrolytic tank is communicated with the circulating tank, the circulating tank is communicated with the etching production line, the etching production line is communicated with the etching waste liquid collecting tank, the etching waste liquid collecting tank is communicated with the etching waste liquid storage tank, and the etching waste liquid storage tank is communicated with the ionic membrane electrolytic tank.
Furthermore, the ion membrane electrolytic cell comprises an anode region and a cathode region, the circulating cell comprises an anode circulating cell and a cathode circulating cell, the anode circulating cell is communicated with the anode region, the cathode circulating cell is communicated with the cathode region, and an etching solution parameter monitoring device is arranged on the anode circulating cell.
The beneficial effects of the utility model reside in that: the utility model discloses an ionic membrane electrolytic cell is through adopting resistance detection device to measure the resistance between titanium net and the adjacent negative plate, is less than the setting value when resistance, produces alarm signal, and when resistance be zero, audible-visual annunciator can send audible-visual annunciator, and the operator in time handles, can prevent like this that the ionic membrane from impaling.
The utility model discloses an ion membrane electrolysis trough can produce the harm with the prevention copper nail by the early warning copper nail, simple structure, and convenient to use is with low costs.
The utility model discloses an ionic membrane copper recovery plant adopts ionic membrane electrolysis technology to regenerate etching solution and retrieve copper, this technology is an online regeneration technology, be about to electrolysis regeneration plant and etching machine and establish ties, regeneration reaction and etching reaction this to each other reversible reaction cycle in proper order go on, but regeneration back etching solution cycle use, regeneration liquid medicine stability is good, the etching factor is qualified, can save oxidant 70-90% after the retrieval and utilization, save hydrochloric acid 50-70%, reduce 70% etching waste liquid and discharge, equipment stable performance, the operation is maintained simply, degree of automation is high, after with etching line interconnect, the automatic cycle function, do not influence production in the installation and debugging process, the installation and debugging finishes and can put into use.
Drawings
Fig. 1 is a schematic structural diagram of the ion membrane electrolyzer of the present invention.
The reference signs are: the device comprises a tank body 1, a cathode plate 2, an anode plate 3, an anode ion membrane 4, a titanium mesh 5, a resistance detection device 6 and an audible and visual alarm 7.
Detailed Description
In order to facilitate understanding of those skilled in the art, the present invention will be further described with reference to the following examples and the accompanying fig. 1, which are not intended to limit the present invention.
See figure 1, an ion membrane electrolytic cell, including cell body 1, be equipped with two at least negative plates 2 and at least one positive pole box in the cell body 1, negative plate 2 sets up with positive pole box interval, and positive pole box includes support frame, anode plate 3 and two positive pole ionic membrane 4, and anode plate 3 pegs graft in the support frame, and two positive pole ionic membrane 4 are located the both sides of anode plate 3, the support frame is made by titanium net 5, and the titanium net 5 of support frame both sides is connected through resistance detection device 6 electricity with adjacent negative plate 2, and resistance detection device 6 electricity is connected with audible-visual annunciator 7. The anode ion membrane 4 and the support frame are fastened by titanium screws. The support frame is made of a titanium mesh 5, and is corrosion-resistant, conductive and high in strength.
The utility model discloses an ionic membrane electrolytic cell is through adopting resistance detection device 6 to measure the resistance between titanium net 5 and the adjacent negative plate 2, is less than the setting value when resistance, produces alarm signal, and when resistance be zero, audible-visual annunciator 7 sends audible-visual annunciator, and the operator in time handles, can prevent like this that the ionic membrane from impaling.
The design principle of the ion membrane electrolytic cell of the utility model is as follows: when having the copper nail, the distance of ionic membrane and copper nail can diminish, and conventional distance is 40 millimeters, if add a sensor on the ionic membrane, can detect this distance and report to the police, just can accomplish the early warning function. To implement this sensor, various possible ways of photothermal-electromagnetic analysis were analyzed, and it was found that electrical resistance should be achievable and easily achievable. The resistance has a direct relation with the distance, the distance is shortened, and the resistance is reduced. And detecting the change value of the resistance, so that the growth condition of the copper nail can be preliminarily judged. Under the limit condition, the copper nail contacts the ionic membrane, the resistance is zero, and at the moment, the sound-light alarm can be sent out, so that the operator can timely process the ionic membrane. This prevents the ionomer membrane from being punctured.
The titanium mesh 5 is connected to the cathode copper plate, and copper is easily plated on the titanium mesh 5, so that a positive voltage is maintained on the titanium mesh 5 with respect to the cathode. So that no copper is deposited on the titanium mesh 5. For a typical period of time, a positive voltage is maintained with respect to the cathode on the titanium mesh 5. So that no copper is deposited on the titanium mesh 5 and even the copper layer on the titanium mesh 5 will dissolve. The titanium mesh 5 and cathode copper remain connected for a specified test period, such as every 5 minutes for 2 seconds.
The ionic membrane copper recovery equipment is the ionic membrane electrolytic cell.
In this embodiment, the ionic membrane copper recovery equipment further includes a circulation tank, an etching production line, an etching waste liquid collecting tank, and an etching waste liquid storage tank, wherein the ionic membrane electrolytic tank is communicated with the circulation tank, the circulation tank is communicated with the etching production line, the etching production line is communicated with the etching waste liquid collecting tank, the etching waste liquid collecting tank is communicated with the etching waste liquid storage tank, and the etching waste liquid storage tank is communicated with the ionic membrane electrolytic tank.
In this embodiment, the ion membrane electrolytic cell includes an anode region and a cathode region, the circulation tank includes an anode circulation tank and a cathode circulation tank, the anode circulation tank is communicated with the anode region, the cathode circulation tank is communicated with the cathode region, and an etching solution parameter monitoring device is installed on the anode circulation tank.
The structure of the ionic membrane copper recovery device adopted by the utility model is consistent with the structure disclosed in the Chinese invention patent with the application number of 201710030250.3, and is not repeated herein.
The above-mentioned embodiment is the utility model discloses the implementation of preferred, in addition, the utility model discloses can also realize by other modes, not deviating from the utility model discloses any obvious replacement is all within the protection scope under the prerequisite of design.

Claims (4)

1. The utility model provides an ion exchange membrane electrolytic cell, includes the cell body, is equipped with two at least negative plates and at least one positive pole box in the cell body, and negative plate and positive pole box interval set up, and the positive pole box includes support frame, anode plate and two positive pole ionic membrane, and the anode plate is pegged graft in the support frame, and two positive pole ionic membrane are located the both sides of anode plate, its characterized in that: the support frame is made by the titanium net, and the titanium net of support frame both sides is connected through resistance detection device electricity with adjacent negative plate, and resistance detection device electricity is connected with audible-visual annunciator.
2. The utility model provides an acid etching solution regeneration recycles copper recovery plant which characterized in that: the copper recovery plant comprises the ionic membrane electrolysis cell of claim 1.
3. The apparatus for recycling copper from acidic etching solution according to claim 2, wherein: the copper recovery equipment further comprises a circulating tank, an etching production line, an etching waste liquid collecting cylinder and an etching waste liquid storage tank, wherein the ion membrane electrolytic tank is communicated with the circulating tank, the circulating tank is communicated with the etching production line, the etching production line is communicated with the etching waste liquid collecting cylinder, the etching waste liquid collecting cylinder is communicated with the etching waste liquid storage tank, and the etching waste liquid storage tank is communicated with the ion membrane electrolytic tank.
4. The apparatus for recycling copper from acidic etching solution according to claim 3, wherein: the ion membrane electrolytic cell comprises an anode region and a cathode region, the circulating cell comprises an anode circulating cell and a cathode circulating cell, the anode circulating cell is communicated with the anode region, the cathode circulating cell is communicated with the cathode region, and an etching solution parameter monitoring device is arranged on the anode circulating cell.
CN202021684480.5U 2020-08-13 2020-08-13 Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution Active CN213142227U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202021684480.5U CN213142227U (en) 2020-08-13 2020-08-13 Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202021684480.5U CN213142227U (en) 2020-08-13 2020-08-13 Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution

Publications (1)

Publication Number Publication Date
CN213142227U true CN213142227U (en) 2021-05-07

Family

ID=75737439

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202021684480.5U Active CN213142227U (en) 2020-08-13 2020-08-13 Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution

Country Status (1)

Country Link
CN (1) CN213142227U (en)

Similar Documents

Publication Publication Date Title
RU2004102511A (en) ELECTROLYSIS CELL FOR COMPLETING THE CONCENTRATION OF METAL IONS IN ELECTRODEPOSITION METHODS
CN202945326U (en) Acidic waste etching solution recycling system
Pretorius, WA, Johannes, WG & Lempert Electrolytic iron flocculant production with a bipolar electrode in series arrangement
Yap et al. An electrogenerative process for the recovery of gold from cyanide solutions
CN105016431A (en) Method and apparatus for removal and recovering of heavy metal ions from wastewater
CN106623398B (en) Ferric salt reinforced electrodynamic remediation device for heavy metal pollution of electronic waste dismantling field
CN208279439U (en) A kind of organic ammonia nitrogen waste water electrolytic processing apparatus with high salt
CN202272954U (en) System for acid chloride etching liquid cycle regeneration and metallic copper recycling
CN201534880U (en) Device for electrolyzing and recycling copper from low-concentration waste liquid with copper generated from microetching and pickling
CN109534455A (en) A kind of electrochemical method of low-consumption high-efficiency processing heavy metal wastewater thereby
CN203976921U (en) The circulation of acid copper chloride etching liquid electrolytic regeneration and copper coin retrieving arrangement
CN106637216A (en) Acidic etching liquid regeneration reuse copper recycling device
CN213142227U (en) Ion membrane electrolytic cell and copper recovery equipment for regeneration and recycling of acidic etching solution
CN206529526U (en) A kind of acidic etching liquid regeneration cycle uses copper reclaimer
CN109097792A (en) A kind of electrolysis unit from low concentration cupric cyanide barren solution recycling copper and cyanide
CN104947155A (en) Process for recovering copper from waste circuit board to prepare high purity and high strength copper foil based on electrochemical method
CN102912351B (en) Electrolytic cell for acidic etching liquid in-situ regeneration technology
CN212102127U (en) Device for coprocessing electroplating sludge and hydrochloric acid pickling waste liquid by using electrolytic method
CN209619472U (en) A kind of device recycling nickel from nickel-containing waste water
CN210523390U (en) Electronic prosthetic devices of compound heavy metal contaminated soil
CN103590070B (en) For the structure of copper bar of Electrode connection in electrolytically etching liquid
CN109205878A (en) A kind of electric flocculation device and method handling effluent containing heavy metal ions
CN205892820U (en) System for ammonia nitrogen in electrolytic oxidation method processing ammonia nature copper chloride waste water
CN204643916U (en) A kind of standard zero polar distance electrolytic bath for water treatment
CN202705559U (en) Copper bar structure for electrode connection in electrical etching liquid

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant